Compositions and methods of producing methionine

ABSTRACT

Described herein are microorganisms that produce methionine and related products from endogenous genes in a transsulfuration pathway, as well as from exogenous genes providing a direct sulfhydrylation pathway. Novel genes that are useful for methionine and SAMe production are disclosed.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is the National Stage of International Application No. PCT/US2007/00914, filed Apr. 11, 2007.

REFERENCE TO SEQUENCE LISTING SUBMITTED ELECTRONICALLY VIA EFS-WEB

The content of the electronically submitted sequence listing (Name: 2511_(—)0050000SEQIDLisitng_AmendUpdate.ascii.txt; Size: 64,460 bytes; and Date of Creation: Oct. 3, 2012) is incorporated by reference in its entirety.

FIELD

Disclosed are compositions, such as microorganisms, enzymes, and chemicals, as well as methods for using the same for producing methionine and related products.

BACKGROUND

Methionine is an essential amino acid in the animal diet. Methionine has been produced synthetically for an extensive period of time by various multi-step chemical synthesis employing acrolein, methyl mercaptan and cyanide as starting materials. There are two product forms: D,L methionine and its hydroxyanalog. D-methionine is converted into the required L-isomer in vivo, unlike all other amino acids. The market for feed-grade methionine has been reported to be improving due to increased demand in poultry and more recently swine feed supplementation. The ability of the leading methionine producers (Degussa AG, Adisseo, and Novus) to meet the market demand hinges on raw material supplies. The intermediates acrolein and methyl mercaptan must be converted into 3-methylthiopropionaldehyde (MMP) and further into methionine using hydrogen cyanide. All three producers have plans for expansion of their methionine production facilities and integration with raw material production as well (Chem. Marketing Reporter Apr. 7, 2003).

The biosynthetic pathways for methionine (a member of the aspartate family of amino acids) have been studied in a number of organisms and show similarities as well as differences. The first dedicated step, acylation of homoserine is catalyzed by homoserine acyltransferase, and is ubiquitous in all organisms despite differences in the transferred acyl group. The product of metA catalysis is either acetylhomoserine or succinylhomoserine. Acylhomoserine is then converted to homocysteine via a transsulfuration or a direct sulfhydrylation pathway. Both pathways have been reported to be present and functional in yeast, fungi, green plants and the bacterium Corynebacterium glutamicum. E. coli possesses only the transsulfuration pathway. The transsulfuration pathway goes through cystathionine as an intermediate and utilizes cysteine as a sulfur donor. The direct sulfhydrylation pathway involves the direct incorporation of sulfide to the acylhomoserine. The last step in the pathway involves the conversion of homocysteine to methionine catalyzed by an homocysteine methyltransferase, encoded by the metE or metH genes.

Other important amino acids, such as lysine, threonine, and tryptophan are produced via fermentation for use in animal feed. Therefore, these amino acids can be made using glucose and other renewable resources as starting materials. Unfortunately, the production of methionine via fermentation has not been as successful and the chemical synthesis of methionine is still used today. This is in part due to the lack of an efficient engineered biosynthetic pathway for methionine production, and a suitable production host.

The following disclosure provides an improved methionine biosynthetic pathway, as well as production host.

SUMMARY

The production of methionine and related products, such as S-adenosylmethionine (SAMe), by fermentation are described herein. Microorganisms that have been genetically engineered to include recombinant DNA molecules and produce methionine are also described.

A microorganism that includes an exogenous nucleic acid sequence encoding a peptide having direct sulfhydrylation activity (EC 2.5.1.49, EC 4.2.99-), and endogenous nucleic acid sequences encoding peptides having transsulfuration activity (EC 2.5.1.48 and 4.4.1.8) is described. This microorganism can produce methionine and related products. In some examples, the microorganism can have at least 0.1, 1, 2, 5, 10, 50, 75, 90, or at least 100 g/L extracellular concentration of methionine or SAMe.

In some examples, the presence of more than one methionine biosynthetic pathway allows the organism to produce more methionine than would be produced in the absence of the exogenous nucleic acid sequence encoding the peptide having direct sulfhydrylation activity.

In other examples, more than two methionine biosynthetic pathways can be active in the organism. In these examples one or more exogenous nucleic acid sequences encode for peptides having direct sulfhydrylation activity. One of these peptides can use O-succinylhomoserine as a substrate and another peptide can use O-acetylhomoserine as a substrate.

In some examples, the microorganisms engineered to make methionine and related products, such as SAMe, produce at least 10% of the methionine from transsulfuration biosynthetic pathway activity. In other examples they produce at least 20, 30, 40, or at least 50% of the product from the transsulfuration biosynthetic pathway activity.

In some examples, the microorganisms engineered to make methionine and related products, such as SAMe, produce at least 10% of the methionine from direct sulfhydrylation biosynthetic pathway activity. In other examples they produce at least 20, 30, 40, or at least 50% of the product from the direct sulfhydrylation biosynthetic pathway activity.

In some examples, the microorganism engineered to make methionine and related products additionally has been engineered to attenuate the activity of a peptide encoded by a gene such as metD, metK, meg thrB, serA or combinations thereof. In other examples, the microorganism is additionally engineered to over express one or more genes, such as the metA, metB, metC, metE, metY, metZ, metX, metH, cysPWUA, cysD, cysN, cysC, cysH, cysI, cysJ, cysG, csyK and cysM genes.

Methods of making methionine and SAMe are also provided. These methods include culturing the microorganism engineered to make methionine and related products and isolating the products. In some examples the microorganism can be E. coli, Pseudomonas sp., or Corynebacterium glutamicum.

Also described herein are novel nucleic acid sequences and their corresponding amino acid sequences (SEQ ID NOS: 1 and 2). These nucleic acid sequences, as well as fragments and variants of these nucleic acid sequences, are useful for producing peptides in recombinant microorganisms. The peptides are useful, inter alia, for producing methionine and SAMe. The peptides, variants thereof, and fragments thereof, are also useful for producing specific binding agents such as antibodies.

A method of improving sulfur assimilation by bypassing the phosphoadenylylsulfate (PAPS) intermediate is also disclosed. This method can be used with any microorganism used to produce methionine. The method is accomplished by introducing into a microorganism a recombinant nucleic acid sequence that allows for the over expression of one or more adenylyl sulfate reductases (EC 1.8.9.92 or 1.8.4.9). Over expression can be from introducing recombinant nucleic acid sequences altering or introducing new control elements, such as promoters or enhancers, that cause an increase in the production of endogenous adenylyl sulfate reductase or the recombinant nucleic acid sequence can encode adenylyl sulfate reductase.

These and other aspects of the disclosure are apparent from the following detailed description and illustrative examples.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1. is a diagram showing three general pathways used by various microorganisms to produce methionine. All of the pathways rely in part upon the use of aspartate as a precursor for methionine production. Aspartate is converted through multiple steps to homoserine, homoserine is converted to O-acetyl homoserine or O-succinyl homoserine by MetA or MetX. Some microorganisms, such as E. coli and Pseudomonas sp. utilize MetA polypeptides to make O-succinyl homoserine while other microorganisms such as Corynebacterium and Leptospira sp. use MetX to make O-acetyl homoserine. O-succinyl homoserine and O-acetyl homoserine can be then either directly converted to homocysteine through sulfhydrylation, or they can be converted to homocysteine through transsulfuration (both of which reactions are described in more detail herein). Enzymes associated with transsulfuration are identified with two asterisks (**), and enzymes associated with sulfhydrylation are identified with a single asterisk (*).

FIG. 2 is a graph showing accumulation of methionine in TF4076BJF, with only transsulfuration activity (TF4076BJF), only sulfhydrylation activity (TF4076BJF-A), or both simultaneously (TF4076BJF metYX(Lm).

FIG. 3 shows a schematic representation of the screening methodology used to identify metA mutants that are resistant to feed back inhibition. (The product accumulated in each case is shown in the shadowed oval).

FIG. 4 shows a time course of methionine accumulation produced by a strain expressing feedback inhibition resistant metA genes.

FIG. 5 shows a model of methionine transport in E. coli.

FIG. 6 shows the native sulfur assimilation pathway and a novel alternative one.

SEQUENCE LISTING

The nucleic and amino acid sequences listed in the accompanying sequence listing are shown using standard letter abbreviations for nucleotide bases, and three-letter code for amino acids. Only one strand of each nucleic acid sequence is shown, but the complementary strand is understood as included by any reference to the displayed strand.

SEQ ID NOS: 1-10 show nucleic acid sequences and corresponding amino acid sequences of various mutant metA genes derived from E. coli.

SEQ ID NOS: 11 through 34 show various primer sequences used in the Examples.

DETAILED DESCRIPTION Abbreviations and Terms

The following explanations of terms and methods are provided to better describe the present disclosure and to guide those of ordinary skill in the art in the practice of the present disclosure. As used herein, “comprising” means “including”and the singular forms “a” or “an” or “the” include plural references unless the context clearly dictates otherwise. For example, reference to “comprising a cell”includes one or a plurality of such cells, and reference to “comprising the homocysteine synthase peptide” includes reference to one or more homocysteine synthase peptides and equivalents thereof known to those of ordinary skill in the art, and so forth. The term “or” refers to a single element of stated alternative elements or a combination of two or more elements, unless the context clearly indicates otherwise. For example, the phrase “homocysteine synthase activity or cystathionine γ-synthase activity” refers to homocysteine synthase activity, cystathionine γ-synthase activity, or a combination of both homocysteine synthase activity, and cystathionine γ-synthase activity.

Unless explained otherwise, all technical and scientific terms used herein have the same meaning as commonly understood to one of ordinary skill in the art to which this disclosure belongs. Although methods and materials similar or equivalent to those described herein can be used in the practice or testing of the present disclosure, suitable methods and materials are described below. The materials, methods, and examples are illustrative only and not intended to be limiting. Other features and advantages of the disclosure are apparent from the following detailed description and the claims.

Accession Numbers: The accession numbers throughout this description are derived from the NCBI database (National Center for Biotechnology Information) maintained by the National Institute of Health, U.S.A. The accession numbers are as provided in the database on Feb. 20, 2007.

Enzyme Classification numbers (EC.): The EC numbers provided throughout this description are derived from the KEGG Ligand database, maintained by the Kyoto Encyclopedia of Genes and Genomics, sponsored in part by the University of Tokyo. The EC numbers are as provided in the database on Feb. 20, 2007.

Attenuate: To lessen the impact, activity or strength of something. In one example, the sensitivity of a particular enzyme to feedback inhibition or inhibition caused by a composition that is not a product or a reactant (non-pathway specific feedback) is lessened such that the enzyme activity is not impacted by the presence of a compound. For example, the metA gene and its corresponding amino acid sequence (such as the exemplary sequences provided inSEQ ID NOS: 2) show several mutations that attenuate its feedback inhibition sensitivity. The attenuation of MetA sensitivity is described in more detail in Example 3.B. In another example, an enzyme that is less active can be referred to as attenuated.

cDNA (complementary DNA): A piece of DNA lacking internal, non-coding segments (introns) and regulatory sequences which determine transcription. cDNA can be synthesized by reverse transcription from messenger RNA extracted from cells.

Deletion: The removal of one or more nucleotides from a nucleic acid molecule or one or more amino acids from a protein, the regions on either side being joined together.

Detectable: Capable of having an existence or presence ascertained. For example, production of a product from a reactant, for example, the production of O-succinylhomoserine or homocysteine, is detectable if the signal generated from the product or the reactant, is strong enough to be measured.

Direct sulfhydrylation activity: the ability to react OSHS or OAHS directly with S²⁻ to produce homocysteine. Peptides having this activity include for example, homocysteine synthases (EC 4.2.99.-, EC 2.5.1.49) which are encoded by genes such as metZ and metY.

DNA: Deoxyribonucleic acid. DNA is a long chain polymer which includes the genetic material of most living organisms (some viruses have genes including ribonucleic acid, RNA). The repeating units in DNA polymers are four different nucleotides, each of which includes one of the four bases, adenine, guanine, cytosine and thymine bound to a deoxyribose sugar to which a phosphate group is attached. Triplets of nucleotides, referred to as codons, in DNA molecules code for amino acid in a peptide. The term codon is also used for the corresponding (and complementary) sequences of three nucleotides in the mRNA into which the DNA sequence is transcribed.

Endogenous: As used herein with reference to a nucleic acid molecule and a particular cell or microorganism refers to a nucleic acid sequence or peptide that is in the cell and was not placed in the cell using recombinant engineering techniques. For example, a gene that was in the cell when the cell was originally isolated from nature. A gene is still considered endogenous if the control sequences, such as a promoter or enhancer sequences that activate transcription or translation have been altered through recombinant techniques.

Exogenous: As used herein with reference to a nucleic acid molecule and a particular cell refers to any nucleic acid molecule that does not originate from that particular cell as found in nature. Thus, a non-naturally-occurring nucleic acid molecule is considered to be exogenous to a cell once introduced into the cell. A nucleic acid molecule that is naturally-occurring also can be exogenous to a particular cell. For example, an entire coding sequence isolated from cell X is an exogenous nucleic acid with respect to cell Y once that coding sequence is introduced into cell Y, even if X and Y are the same cell type.

Expression: The process by which a gene's coded information is converted into the structures and functions of a cell, such as a protein, transfer RNA, or ribosomal RNA. Expressed genes include those that are transcribed into mRNA and then translated into protein and those that are transcribed into RNA but not translated into protein (for example, transfer and ribosomal RNAs).

Functional Deletion: A mutation, partial or complete deletion, insertion, or other variation made to a gene sequence which reduces or inhibits production of the gene product, or renders the gene product non-functional. For example, functional deletion of metJ in E. coli reduces the repression of the methionine biosynthetic pathway. In another example, functional deletion of thrB in E. coli reduces the use of homoserine in the threonine biosynthetic pathway. In some instances a functional deletion is described as a knock out mutation.

Isolated: An “isolated” biological component (such as a nucleic acid molecule, protein, or cell) has been substantially separated or purified away from other biological components in which the component naturally occurs, such as other chromosomal and extrachromosomal DNA and RNA, and proteins. Nucleic acid molecules and proteins that have been “isolated” include nucleic acid molecules and proteins purified by standard purification methods. The term also embraces nucleic acid molecules and proteins prepared by recombinant expression in a host cell as well as chemically synthesized nucleic acid molecules and proteins.

In one example, isolated refers to a naturally-occurring nucleic acid molecule that is not immediately contiguous with both of the sequences with which it is immediately contiguous (one on the 5′ end and one on the 3′ end) in the naturally-occurring genome of the organism from which it is derived.

Nucleic acid molecule: Encompasses both RNA and DNA molecules including, without limitation, cDNA, genomic DNA, and mRNA. Includes synthetic nucleic acid molecules, such as those that are chemically synthesized or recombinantly produced. The nucleic acid molecule can be double-stranded or single-stranded. Where single-stranded, the nucleic acid molecule can be the sense strand or the antisense strand. In addition, nucleic acid molecule can be circular or linear.

Operably linked: A first nucleic acid sequence is operably linked with a second nucleic acid sequence when the first nucleic acid sequence is placed in a functional relationship with the second nucleic acid sequence. For instance, a promoter is operably linked to a coding sequence if the promoter affects the transcription or expression of the coding sequence. Generally, operably linked DNA sequences are contiguous and, where necessary to join two protein coding regions, in the same reading frame. Configurations of separate genes that are transcribed in tandem as a single messenger RNA are denoted as operons. Thus placing genes in close proximity, for example in a plasmid vector, under the transcriptional regulation of a single promoter, constitutes a synthetic operon.

ORF (open reading frame): A series of nucleotide triplets (codons) coding for peptides, polypeptides or amino acids without any termination codons. These sequences are usually translatable into a peptide.

Purified: The term purified does not require absolute purity; rather, it is intended as a relative term. Thus, for example, a purified peptide preparation, such as a succinylCoA homoserine acyltransferase, or a homocysteine synthase preparation, is one in which the peptide is more concentrated than the peptide is in its environment within a cell. For example, a purified peptide is one that is substantially separated from cellular components (nucleic acids, lipids, carbohydrates, and other peptides) that may accompany it. In another example, a purified peptide preparation is one in which the peptide is substantially-free from contaminants, such as those that might be present following chemical synthesis of the peptide.

In one example, a peptide is purified when at least about 50% by weight of a sample is composed of the peptide, for example when at least about 60%, 70%, 80%, 85%, 90%, 92%, 95%, 98%, or 99% or more of a sample is composed of the peptide. Examples of methods that can be used to purify a peptide, include, but are not limited to the methods disclosed in Sambrook et al. (Molecular Cloning: A Laboratory Manual, Cold Spring Harbor, New York, 1989, Ch. 17). Protein purity can be determined by, for example, polyacrylamide gel electrophoresis of a protein sample, followed by visualization of a single peptide band upon staining the polyacrylamide gel; high-pressure liquid chromatography; sequencing; or other conventional methods.

Recombinant: A recombinant nucleic acid molecule or protein is one that has a sequence that is not naturally occurring, has a sequence that is made by an artificial combination of two otherwise separated segments of sequence, or both. This artificial combination can be achieved, for example, by chemical synthesis or by the artificial manipulation of isolated segments of nucleic acid molecules or proteins, such as genetic engineering techniques. Recombinant is also used to describe nucleic acid molecules that have been artificially manipulated, but contain the same regulatory sequences and coding regions that are found in the organism from which the nucleic acid was isolated.

Sequence identity/similarity: The identity/similarity between two or more nucleic acid sequences, or two or more amino acid sequences, is expressed in terms of the identity or similarity between the sequences. Sequence identity can be measured in terms of percentage identity; the higher the percentage, the more identical the sequences are. Sequence similarity can be measured in terms of percentage similarity (which takes into account conservative amino acid substitutions); the higher the percentage, the more similar the sequences are. Homologs or orthologs of nucleic acid or amino acid sequences possess a relatively high degree of sequence identity/similarity when aligned using standard methods.

Methods of alignment of sequences for comparison are well known in the art. Various programs and alignment algorithms are described in: Smith & Waterman, Adv. Appl. Math. 2:482, 1981; Needleman & Wunsch, J. Mol. Biol. 48:443, 1970; Pearson & Lipman, Proc. Natl. Acad. Sci. USA 85:2444, 1988; Higgins & Sharp, Gene, 73:237-44, 1988; Higgins & Sharp, CABIOS 5:151-3, 1989; Corpet et al., Nuc. Acids Res. 16:10881-90, 1988; Huang et al. Computer Appls. in the Biosciences 8, 155-65, 1992; and Pearson et al., Meth. Mol. Bio. 24:307-31, 1994. Altschul et al., J. Mol. Biol. 215:403-10, 1990, presents a detailed consideration of sequence alignment methods and homology calculations.

The NCBI Basic Local Alignment Search Tool (BLAST) (Altschul et al., J. Mol. Biol. 215:403-10, 1990) is available from several sources, including the National Center for Biological Information (NCBI, National Library of Medicine, Building 38A, Room 8N805, Bethesda, Md. 20894) and on the Internet, for use in connection with the sequence analysis programs blastp, blastn, blastx, tblastn and tblastx. Additional information can be found at the NCBI web site.

BLASTN is used to compare nucleic acid sequences, while BLASTP is used to compare amino acid sequences. To compare two nucleic acid sequences, the options can be set as follows: -i is set to a file containing the first nucleic acid sequence to be compared (such as C:\seq1.txt); -j is set to a file containing the second nucleic acid sequence to be compared (such as C:\seq2.txt); -p is set to blastn; -o is set to any desired file name (such as C:\output.txt); -q is set to −1; -r is set to 2; and all other options are left at their default setting. For example, the following command can be used to generate an output file containing a comparison between two sequences: C:\B12seq -i c:\seq1.txt -j c:\seq2.txt -p blastn -o c:\output.txt -q −1 -r 2.

To compare two amino acid sequences, the options of B12seq can be set as follows: -i is set to a file containing the first amino acid sequence to be compared (such as C:\seq1.txt); -j is set to a file containing the second amino acid sequence to be compared (such as C:\seq2.txt); -p is set to blastp; -o is set to any desired file name (such as C:\output.txt); and all other options are left at their default setting. For example, the following command can be used to generate an output file containing a comparison between two amino acid sequences: C:\B12seq c:\seq1.txt -j c:\seq2.txt -p blastp -o c:\output.txt. If the two compared sequences share homology, then the designated output file will present those regions of homology as aligned sequences. If the two compared sequences do not share homology, then the designated output file will not present aligned sequences.

Once aligned, the number of matches is determined by counting the number of positions where an identical nucleotide or amino acid residue is presented in both sequences. The percent sequence identity is determined by dividing the number of matches either by the length of the sequence set forth in the identified sequence, or by an articulated length (such as 100 consecutive nucleotides or amino acid residues from a sequence set forth in an identified sequence), followed by multiplying the resulting value by 100. For example, a nucleic acid sequence that has 1166 matches when aligned with a test sequence having 1554 nucleotides is 75.0 percent identical to the test sequence (1166÷1554*100=75.0). The percent sequence identity value is rounded to the nearest tenth. For example, 75.11, 75.12, 75.13, and 75.14 are rounded down to 75.1, while 75.15, 75.16, 75.17, 75.18, and 75.19 are rounded up to 75.2. The length value will always be an integer.

For comparisons of amino acid sequences of greater than about 30 amino acids, the Blast 2 sequences function is employed using the default BLOSUM62 matrix set to default parameters, (gap existence cost of 11, and a per residue gap cost of 1). Homologs are typically characterized by possession of at least 70% sequence identity counted over the full-length alignment with an amino acid sequence using the NCBI Basic Blast 2.0, gapped blastp with databases such as the nr or swissprot database. Queries searched with the blastn program are filtered with DUST (Hancock and Armstrong, 1994, Comput. Appl. Biosci. 10:67-70). Other programs use SEG. In addition, a manual alignment can be performed. Proteins with even greater similarity will show increasing percentage identities when assessed by this method, such as at least 75%, at least 80%, at least 85%, at least 90%, at least 95%, at least 97%, or at least 99% sequence identity to the subject sequence (i.e. sequence identified by accession number or the like), while retaining the activity of the subject sequence. In some examples, the subject sequence will have greater activity than that of the native sequence and in yet other examples it will be less active.

When aligning short peptides (fewer than approximately 30 amino acids), the alignment should be performed using the Blast 2 sequences function, employing the PAM30 matrix set to default parameters (open gap 9, extension gap 1 penalties). Proteins with even greater similarity to the reference sequence will show increasing percentage identities when assessed by this method, such as at least 60%, 70%, 75%, 80%, 85%, 90%, 95%, 98%, 99% sequence identity. When less than the entire sequence is being compared for sequence identity, homologs will typically possess at least 75% sequence identity over short windows of 10-20 amino acids, and can possess sequence identities of at least 85%, 90%, 95% or 98% depending on their identity to the reference sequence. Methods for determining sequence identity over such short windows are described at the NCBI web site.

Nucleic acid sequences that do not show a high degree of identity may nevertheless encode identical or similar (conserved) amino acid sequences, due to the degeneracy of the genetic code. Changes in a nucleic acid sequence can be made using this degeneracy to produce multiple nucleic acid molecules that all encode substantially the same protein. Such homologous nucleic acid sequences can, for example, possess at least 60%, at least 70%, at least 80%, at least 90%, at least 95%, at least 98%, or at least 99% sequence identity to a subject sequence (sequences identified by accession number or the like).

One of skill in the art will appreciate that these sequence identity ranges are provided for guidance only; it is possible that strongly significant homologs could be obtained that fall outside the ranges provided.

Transformed cell: A cell into which a nucleic acid molecule has been introduced, such as a succinylCoA homoserine acyltransferase, or a homocysteine synthase nucleic acid molecule, for example by molecular biology techniques. Transformation encompasses all techniques by which a nucleic acid molecule can be introduced into such a cell, including, but not limited to, transfection with viral vectors, conjugation, transformation with plasmid vectors, and introduction of naked DNA by electroporation, lipofection, and particle gun acceleration.

Transsulfuration activity: An activity that produces methionine or SAMe via the intermediate, cystathionine. Peptides having this activity include cystathionine γ synthase (EC 2.5.1.48) and cystathionine β lyase (EC 4.4.1.8), these peptides are encoded by the genes metB and metC, respectively. Any combination of cystathionine y synthase (EC 4.2.99.9) and cystathionine β lyase (EC 4.4.1.8) peptides can be used to allow a microorganism to possess transsulfuration activity.

Under conditions that permit product production: Any fermentation conditions that allow a microorganism to produce a desired product, such as methionine or SAMe. Conditions usually include temperature, aeration, and medium. The medium can be a broth or a gel. Generally, the medium includes a carbon source such as glucose, fructose, cellulose, or the like that can be metabolized by the microorganism directly, or enzymes can be used in the medium to facilitate metabolizing the carbon source. To determine if culture conditions permit product production, the microorganism can be cultured for 24, 36, or 48 hours and a sample can be taken. The cells in the sample can be then tested for the presence of the desired product. For example when testing for the presence of methionine or SAMe the assays provided in the Examples section may be used.

Vector: A nucleic acid molecule as introduced into a cell, thereby producing a transformed cell. A vector can include nucleic acid sequences that permit it to replicate in the cell, such as an origin of replication. A vector can also include one or more selectable marker genes and other genetic elements known in the art.

DETAILED DESCRIPTION

I. Methionine Production Pathways

As shown in FIG. 1, many biosynthetic pathways can be used to produce methionine or its intermediates such as aspartyl phosphate, aspartate semialdehyde homoserine, O-succinylhomoserine (OSHS), O-acetylhomoserine (OAHS), cystathionine, homocysteine, methionine, and S-adenosyl methionine (SAMe). For the purposes of this disclosure an intermediate can be referred to as a reactant or a product, depending upon context. For example, when discussing the conversion of aspartate to aspartyl phosphate using an aspartate kinase, the aspartate is the reactant and the aspartyl phosphate is the product. Similarly, when the description describes the conversion of aspartyl phosphate to aspartate semialdehyde using an aspatate semialdehyde dehydrogenase, the aspartyl phosphate is the reactant and the aspartate semialdehyde is the product. One of ordinary skill in the art will appreciate that FIG. 1 shows many biosynthetic pathways because within each enzyme class provided there are many enzymes that can be used to convert a reactant to a product and, therefore, make a pathway. Moreover, these reactions can be carried out in vivo, in vitro, or through a combination of in vivo reactions and in vitro reactions, such as in vitro reactions that include non-enzymatic chemical reactions.

The host microorganism can also be provided intermediates in the pathway by including the intermediates in the fermentation feedstock. Thus, if the biosynthetic pathway is producing less than a desired amount of a given intermediate, that intermediate can be added to the feedstock. This can be done in either a continuous fermentation setting or in a batch fermentation setting.

Those of ordinary skill in the art will recognize that a production host can use carbon sources other than glucose. Alternative carbons sources include for example, sucrose, fructose, cellulose, hemicellulose, starch, or glycerol. When alternative carbon sources are used it may be necessary to include enzymes that will modify the carbon source in the fermentation media.

A. Glucose to Aspartate

Microorganisms generally produce aspartate from glucose. One of ordinary skill in the art will appreciate that there are many methods of increasing the aspartate concentration in production strains. For example, increasing the expression of the enzymes pyruvate carboxylase and phosphoenolpyruvate carboxylase, altering the glyoxylate shunt or eliminating the consumption of pyruvate into other products such as acetate or ethanol.

Alternatively, aspartate can be included in the fermentation feedstock, taken up by the microorganism, and used as a reactant in the methionine biosynthetic pathway.

Aspartate also serves as an intermediate in the lysine, threonine, and asparagine biosynthetic pathways. Therefore, it may be desirable to attenuate or remove (knockout) these pathways, thus allowing more aspartate to be used in the methionine production pathway.

B. Aspartate to Aspartyl Phosphate

Production hosts can be engineered using known polypeptides to produce aspartyl phosphate, or to overproduce aspartyl phosphate. For example, the feed back resistant aspartate kinase described in WO04069996A2 can be used to replace an endogenous aspartate kinase or in addition to an endogenous aspartate kinase.

As used herein, aspartate kinase includes peptides in enzyme classification number (EC) 2.7.2.4, as well as any other peptide capable of catalyzing the conversion of aspartate to aspartyl phosphate. Additionally, one of ordinary skill in the art will appreciate that some aspartate kinase peptides will catalyse other reactions as well, for example some aspartate kinase peptides will accept other substrates in addition to aspartate. Such non-specific aspartate kinase peptides are, therefore, also included. Aspartate kinase sequences are publicly available. For example, GenBank Accession Nos: NZ_AAVY01000022, NC_(—)006958, and NZ_AAWW01000055, disclose aspartate kinase nucleic acid sequences and GenBank Accession Nos: NP_(—)418448, NP_(—)599504 and ZP_(—)01638096 disclose aspartate kinase peptide sequences. Assays for characterizing the aspartate kinase activity of a particular peptide are well known in the art. For example, the assay described by Cohen, G N, Methods in Enzymology, 113:596:600, 1985, can be used to characterize the activity of a specific peptide.

C. Aspartyl Phosphate to Aspartate Semialdehyde

Production hosts can be engineered using known polypeptides to produce aspartate semialdehyde, or to overproduce aspartate semialdehyde. One method of increasing the production of products in the methionine biosynthetic pathway is through over-expression or the expression of a more active form of aspartate semialdehyde dehydrogenase.

As used herein, aspartate semialdehyde dehydrogenase includes aspartate semialdehyde dehydrogenase peptides (EC 1.2.1.11), as well as any other peptide capable of catalyzing the conversion of aspartyl phosphate to aspartate semialdehyde. Additionally, one of ordinary skill in the art will appreciate that some aspartate semialdehyde dehydrogenase peptides will catalyze other reactions as well. For example, some aspartate semialdehyde dehydrogenase peptides will accept other substrates in addition to aspartyl phosphate, and therefore, such non-specific aspartate semialdehyde dehydrogenase peptides are also included. Aspartate semialdehyde dehydrogenase sequences are publicly available. For example, GenBank Accession Nos: NC_(—)006958, NZ_AAVY01000015 and NZ_AAWW01000010 disclose aspartate semialdehyde dehydrogenase nucleic acid sequences and GenBank Accession Nos: NP_(—)417891, NP_(—)599505 and ZP_(—)0164))72 disclose aspartate semialdehyde dehydrogenase peptide sequences. Assays for characterizing the aspartate semialdehyde dehydrogenase activity of a particular peptide are well known in the art. For example, the assay described by Cohen, G N., Methods in Enzymology, 113:600-602, 1985, can be used to characterize the activity of a specific peptide.

D. Aspartate Semialdehyde to Homoserine

Production hosts can be engineered using known polypeptides to produce homoserine, or to overproduce homoserine. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of aspartate semialdehyde dehydrogenase.

As used herein, homoserine dehydrogenase includes homoserine dehydrogenase peptides (EC 1.1.1.3), as well as any other peptide capable of catalyzing the conversion of aspartate semialdehyde to homoserine. Additionally, one of ordinary skill in the art will appreciate that some homoserine dehydrogenase peptides will catalyze other reactions as well, for example some homoserine dehydrogenase peptides will accept other substrates in addition to aspartate semialdehyde. Such non-specific homoserine dehydrogenase peptides are, therefore, also included. Homoserine dehydrogenase peptide sequences are publicly available. For example, GenBank Accession Nos: NC_(—)006958, NZ_AAVY01000013 and NZ_AAWW01000033 disclose homoserine dehydrogenase nucleic acid sequences and GenBank Accession Nos: NP_(—)414543, ZP_(—)01639819 and NP_(—)600409 disclose homoserine dehydrogenase peptide sequences. Assays for characterizing the homoserine dehydrogenase activity of a particular peptide are well known in the art. For example, the assay described by Patte et.al., Biochem. Biophys. Acta 128:426-439, 1966, can be used to characterize the activity of a specific peptide.

E. Homoserine to O-succinylhomoserine (OSHS)

Production hosts can be engineered using known polypeptides to produce O-succinylhomoserine (OSHS), or to overproduce OSHS. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of homoserine O-succinyltransferase peptides, or using a feed back inhibition insensitive form of homoserine O-succinyltransferase peptides.

As used herein, succinylCoA homoserine acyltransferase, includes homoserine O-succinyltransferase peptides (EC 2.3.1.46), as well as any other peptide capable of catalyzing the conversion of homoserine to OSHS. Additionally, one of ordinary skill in the art will appreciate that some homoserine O-succinyltransferase peptides will catalyze other reactions as well, for example some succinylCoA -homoserine acyltransferase peptides will accept other substrates in addition to homoserine. Such non-specific succinylCoA -homoserine acyltransferase peptides are, therefore, also included. Homoserine O-succinyltransferase peptide sequences are publicly available. For example, GenBank Accession No: NZ_AAWW01000055 discloses a homoserine O-succinyltransferase nucleic acid sequence and GenBank Accession No: AAC76983 discloses a homoserine O-succinyltransferase peptide sequence. Assays for characterizing succinylCoA -homoserine acyltransferase activity are well known in the art. For example, the assay described by Lawrence, J. Bacteriol., 109:8-11, 1972, can be used to characterize the activity of a specific peptide. Genes encoding succinylCoA -homoserine acyltransferase peptides are also referred to herein as metA.

F. Homoserine to O-acetylhomoserine (OAHS)

Production hosts can be engineered using known polypeptides to produce O-acetylhomoserine (OAHS), or to overproduce OAHS. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of homoserine O-acetyltransferase peptides (EC 2.3.1.31).

As used herein, homoserine O-acetyltransferase, includes homoserine O-acetyltransferase peptides (EC 2.3.1.31), as well as any other peptide capable of catalyzing the conversion to OAHS. Additionally, one of ordinary skill in the art will appreciate that some homoserine O-acetyltransferase peptides will catalyze other reactions as well, for example some homoserine O-acetyltransferase peptides will accept other substrates in addition to homoserine. Such non-specific homoserine O-acetyltransferase peptides are, therefore, also included. Homoserine O-acetyltransferase peptide sequences are publicly available. For example, GenBank Accession Nos: Y10744 REGION: 2822 . . . 3961, NZ_AAAH02000004 REGION: 166057 . . . 167193 and NZ_AAAY02000081 REGION: complement(11535 . . . 12605) disclose homoserine O-acetyltransferase nucleic acid sequences and GenBank Accession Nos: CAA71733, ZP_(—)00766367 and ZP_(—)00107218 disclose homoserine O-acetyltransferase peptide sequences. Assays for characterizing homoserine O-acetyltransferase activity are well known in the art. For example, the assay described by Lawrence, J. Bacteriol., 109:8-11, 1972, can be used to characterize the activity of a specific peptide. Genes encoding homoserine O-acetyltransferase peptides are also referred to herein as metX.

G. Sulfhydrylation

The production of homocysteine by direct sulfhydrylation is accomplished by homocysteine synthase enzymes, some of these enzymes utilize OSHS as a substrate, and some of utilize OAHS as a substrate. Additionally, some of the enzymes can utilize either OSHS or OAHS as substrates.

1. O-succinylhomoserine (OSHS) to Homocysteine

Production hosts can be engineered using known polypeptides to produce homocysteine, or to overproduce homocysteine. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of homocysteine synthase peptides (EC 4.2.99.-).

As used herein, homocysteine synthase includes homocysteine synthase peptides (EC 4.2.99.-), as well as any other peptide capable of catalyzing the conversion of O-succinylhomoserine (OSHS) to homocysteine. The conversion of OSHS to homocysteine through reaction with sulfide is referred to herein as direct sulfhydrylation. Additionally, one of ordinary skill in the art will appreciate that some homocysteine synthase peptides will catalyze other reactions as well, for example some homocysteine synthase peptides will accept other substrates in addition to OSHS. Such non-specific homocysteine synthase peptides are, therefore, also included. Homocysteine synthase peptide sequences are publicly available. For example, GenBank Accession No: AE004091 discloses a homocysteine synthase (O-succynil-L-homoserine sulfhydrylase) nucleic acid sequences and GenBank Accession No: AAG06495 discloses a homocysteine synthase (O-succynil-L-homoserine sulfhydrylase) amino acid sequence. Assays for characterizing the homocysteine synthase activity of a particular peptide are well known in the art. For example, the assay described by Yamagata, Methods in Enzymology, 143:478, 1987, can be used, with the appropriate substrate, to characterize the activity of a specific peptide. Genes encoding homocysteine synthase peptides are also referred to herein as metZ.

2. O-acetylhomoserine (OAHS) to Homocysteine

Production hosts can be engineered using known polypeptides to produce homocysteine, or to overproduce homocysteine. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of homocysteine synthase peptides (EC 2.5.1.49).

As used herein, homocysteine synthase includes homocysteine synthase peptides (EC 2.5.1.49), as well as any other peptide capable of catalyzing the conversion of O-succinylhomoserine (OAHS) to homocysteine. The conversion of OAHS to homocysteine through reaction with sulfide is referred to herein as direct sulfhydrylation. Additionally, one of ordinary skill in the art will appreciate that some homocysteine synthase peptides will catalyze other reactions as well, for example some homocysteine synthase peptides will accept other substrates in addition to OSHS, for example the homocysteine synthase described in Example 2, below accepts either OAHS or OSHS as a substrate, such non-specific homocysteine synthase peptides are, therefore, also included. Homocysteine synthase peptide sequences that are publicly available. For example, GenBank Accession Nos: AE004091 REGION: 5655648 . . . 5656925, Y10744 REGION: 1485 . . . 2813, NZ_AAAH02000004 REGION: 164536 . . . 165990 and NZ_AAAY02000081 REGION: complement(12750 . . . 14054) disclose homocysteine synthase (O-acetyl-L-homoserine sulfhydrylase) nucleic acid sequences and GenBank Accession Nos: AAG08410, CAA71732, ZP_(—)00766366, and ZP_(—)00107219 disclose homocysteine synthase (O-acetyl-L-homoserine sulfhydrylase) amino acid sequences. Assays for characterizing the homocysteine synthase activity of a particular peptide are well known in the art. For example, the assay described by Yamagata, Methods in Enzymology, 143:478, 1987, can be used, with the appropriate substrate, to characterize the activity of a specific peptide. Genes encoding homocysteine synthase peptides are also referred to herein as metY.

H. Transsulfuration

1. O-succinylhomoserine (OSHS) or Acetylhomoserine (OAHS) to Cystathionine

Production hosts can be engineered using known polypeptides to produce cystathionine, or to overproduce cystathionine. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of cystathionine γ-synthase peptides (EC 2.5.1.48).

As used herein, cystathionine γ-synthase includes cystathionine γ-synthase peptides (EC 2.5.1.48), as well as any other peptide capable of catalyzing the conversion of OSHS or OAHS to cystathionine. Additionally, one of ordinary skill in the art will appreciate that some cystathionine γ-synthase peptides will catalyze other reactions as well, for example some cystathionine γ-synthase peptides will accept other substrates in addition to OSHS or OAHS. Such non-specific cystathionine γ-synthase peptides are, therefore, also included. Cystathionine γ-synthase peptide sequences are publicly available. For example, GenBank Accession Nos: NC_(—)006958, NZ_AAWW01000006 and NC_(—)004129 disclose cystathionine γ-synthase nucleic acid sequences and GenBank Accession Nos: NP_(—)418374, YP_(—)348978 and NP_(—)601979 disclose cystathionine γ-synthase peptide sequences. Assays for characterizing the cystathionine γ-synthase activity of a particular peptide are well known in the art. For example, the assay described in Methods in Enzymology, 17:425-433, 1971, can be used to characterize the activity of a specific peptide. Genes encoding cystathionine γ-synthase peptides are also referred to herein as metB.

2. Cystathionine to Homocysteine

Production hosts can be engineered using known polypeptides to produce homocysteine, or to overproduce homocysteine. One method of increasing the production of products in the methionine biosynthetic pathway is through over expression or the expression of a more active form of cystathionine β-lyase peptides (EC 4.4.1.8).

As used herein, cystathionine β-lyase includes cystathionine β-lyase peptides (EC 4.4.1.8), as well as any other peptide capable of catalyzing the conversion of cystathionine to homocysteine. Additionally, one of ordinary skill in the art will appreciate that some cystathionine β-lyase peptides will catalyze other reactions as well, for example some cystathionine β-lyase peptides will accept other substrates in addition to cystathionine. Such non-specific cystathionine β-lyase peptides are, therefore, also included. Cystathionine β-lyase peptide sequences are publicly available. For example, GenBank Accession Nos: NZ_AAWW01000001, NC_(—)006958 and NZ_AAVY01000004 disclose cystathionine β-lyase nucleic acid sequences and GenBank Accession Nos: NP_(—)746463, YP_(—)226552 and NP 417481 disclose cystathionine β-lyase peptide sequences. Assays for characterizing the cystathionine β-lyase activity of a particular peptide are well known in the art. For example, the assay described in Methods in Enzymology, 143:483-486, 1987, can be used to characterize the activity of a specific peptide. Genes encoding cystathionine β-lyase peptides are also referred to herein as metC.

I. Homocysteine to Methionine

Production hosts can be engineered using known polypeptides to produce methionine, or to overproduce methionine. One method of increasing the production of products, such as methionine or SAMe in the methionine biosynthetic pathway is through over expression or the expression of a more active form of homocysteine methlyase peptides (EC 2.1.1.14 and 2.1.1.13).

As used herein, homocysteine methlyase includes homocysteine methlyase peptides (EC 2.1.1.14, and 2.1.1.13), as well as any other peptide capable of catalyzing the conversion of homocysteine to methionine. Additionally, one of ordinary skill in the art will appreciate that some homocysteine methlyase peptides will catalyze other reactions as well, for example some homocysteine methlyase peptides will accept other substrates in addition to homocysteine. Such non-specific homocysteine methlyase peptides are, therefore, also included. Homocysteine methlyase peptide sequences are publicly available. For example, GenBank Accession Nos: NC_(—)004129, NC_(—)006958 and NC_(—)000913 disclose homocysteine methlyase nucleic acid sequences and GenBank Accession Nos: AP_(—)004520, YP_(—)225791 and CAK16133 disclose homocysteine methlyase peptide sequences. Assays for characterizing homocysteine methlyase activity of a particular peptide are well known in the art. For example, the assay described in Analytical Biochemistry, 228, 323-329, 1995, can be used to characterize the activity of a specific peptide. Genes encoding homocysteine methlyase peptides are also referred to herein as metH or metE.

J. Methionine to S-adenosylmethionine

Production hosts can be engineered using known polypeptides to produce S-adenosylmethionine (SAMe), or to overproduce SAMe. One method of increasing the production of products, in the methionine biosynthetic pathway is through over expression or the expression of a more active form of methionine adenosyltransferase peptides (EC 2.5.1.6). One of ordinary skill in the art will appreciate that in instances where methionine is the desired product, the activity or expression of methionine adenosyltransferase peptides (EC 2.5.1.6) encoded by metK, may be attenuated.

As used herein, methionine adenosyltransferase includes methionine adenosyltransferase peptides (EC 2.5.1.6), as well as any other peptide capable of catalyzing the conversion of methionine to SAMe. Additionally, one of ordinary skill in the art will appreciate that some methionine adenosyltransferase peptides will catalyze other reactions as well, for example some methionine adenosyltransferase peptides will accept other substrates in addition to methionine. Such non-specific methionine adenosyltransferase peptides are, therefore, also included. Methionine adenosyltransferase peptide sequences are publicly available. For example, GenBank Accession Nos: NC_(—)002516, NC_(—)006958 and NC_(—)000913 disclose methionine adenosyltransferase nucleic acid sequences and GenBank Accession Nos: NP_(—)747070, CAI37180 and NP_(—)600817 disclose methionine adenosyltransferase peptide sequences. Assays for characterizing the methionine adenosyltransferase activity of a particular peptide are well known in the art. For example, the assay described in Methods in Enzymology, 94: 219-222, 1983, can be used to characterize the activity of a specific peptide. Genes encoding methionine adenosyltransferase peptides are also referred to herein as metK.

II. Genetic Engineering of Production Strain to Increase Methionine Production

Aspartate production can be increased using any method known in the art. For example, aspartate production can be increased by increasing the amount of oxaloacetate produced by the cells with several different approaches. (Gokam et.al, Appl. Microbiol. Biotechnol., 56:188-95, 2001; Sanchez et.al, Metabolic Eng., 8:209-226, 2006).

The production of product can also be increased by over expressing various genes in the L-methionine biosynthetic pathway. For example, genes such as metA, metB, metC, metE, and metH, cysD, cysN, cysC, cysH, cysI, cysJ, cysK and cysM can be placed under the control of a variety of promoters thus allowing higher amounts of these enzymes to be produced.

The metA gene encodes homoserine succinyltransferase which is the first enzyme in the methionine biosynthesis pathway from homoserine and a regulation point for methionine production. The metA protein is a temperature sensitive protein of 186 amino acid residues with a calculated molecular mass of 35.7 kDa. The metA activity is known to be inhibited by the end-products, methionine and S-adenosylmethionine (Lee et al., J. Biol. Chem. 241:5479-5780, 1966). Feedback inhibition by these two products is synergistic, meaning that low concentrations of each metabolite alone are only slightly inhibitory, while in combination a strong inhibition is exerted. Thus, a production strain could benefit from a feedback inhibition resistant MetA activity.

Another gene that can be attenuated or deleted in the methionine production strain is mea. The peptide encoded by metJ regulates the expression of several genes involved in methionine biosynthesis pathway. The protein encoded by metJ binds to S-adenosyl methionine and represses the metA, metC, and metF genes.

The protein encoded by the metF gene, 5,10-methylenetetrahydrofolate reductase, is involved in the synthesis of N(5)-methyltetrahydrofolate which is a methyl group donor for L-methionine production from homocysteine (Sheppard et al., J. Bacteriol. 181:718-25, 1999). US 2002/0049305 discloses that the production of L-methionine can be improved by increasing the expression of 5, 10-methylenetetrahydrofolate reductase (metF) in Corynebacteria. Accordingly, the engineered microorganisms described herein can also be engineered to increase metF production.

The modulation of the gene metK can also increase methionine and SAMe production. S-adenosylmethionine (SAMe) is the primary methyl group donor in all organisms and is involved in polyamine biosynthesis. SAMe is also known as methionine adenosyltransferase (MAT or MetK, EC 2.5.1.6). MetK catalyzes the only known route for SAMe biosynthesis. The complete tripolyphosphate chain is cleaved from ATP and the sulfonium compound is formed.

The formation of SAMe decreases the concentration of methionine and reduces the activity of the methionine biosynthetic pathway via feed back inhibition of MetA. Hence, functionally deleting or attenuating metK can increase methionine production.

One of ordinary skill in the art will appreciate that the efficiency of sulfur utilization by any cell that is making methionine is important. This is especially true for microorganisms that utilize phosphoadenylylsulfate (PAPS) as an intermediate during sulfur assimilation, because making PAPS requires the expenditure of a-molecule of ATP.

Sulfate is fairly unreactive and must first be converted to a more reactive form in order to be used by the cell. In E. coli sulfate is incorporated in the cell by a periplasmic transport system, composed of three cytoplasmic membrane components and a substrate specific binding protein located in the periplasmic space. The three membrane components of the sulfate permease are encoded by the cysT, cysW, and cysA genes (cysA locus). The products of the cysA locus are regulated in concert with the rest of the sulfate-assimilation pathway as part of the cys regulon. Sulfate is then activated by coupling to a nucleoside to make high-energy nucleoside phosphosulfates via a pathway that appears to be similar in most organisms.

As shown in FIG. 6, a microorganism such as E. coli utilizes a pathway that converts sulfate to adenylylsulfate (APS) using a sulfate adenylyl transferase peptide (EC 2.7.7.4 coded by cysNcysD). The APS is then converted to PAPS by APS kinase (EC 2.7.1.25 encoded by cysC). This step requires one ATP. PAPS is converted to sulfite by a PAPS reductase (EC 1.8.4.8 coded by cysH) and sulfite is reduced to sulfide by NADPH-sulfite reductase (EC1.8.1.2 coded by cysIcysJcysG). The alternate pathway, shown on the right side of FIG. 6, converts APS directly to sulfite using an adenylyl sulfate reductase (EC 1.8.9.92 or 1.8.4.9). One of ordinary skill in the art will appreciate that any adenylyl sulfate reductase that can convert APS to sulfite will work. For example, the adenylyl sulfate reductase from Bacillus subtilis (Accession number CAA04409), or from Pseudomonas aeruginosa (Accession number NP_(—)250447).

Adenylyl sulfate reductase encoding nucleic acid sequences can be introduced into any microorganism used to produce methionine. For example the strains described herein, as well as the strains described in WO2005/108561 and WO2006138689 by Metabolic Explorer, and those described by Kumar and Gomes, Biotechnology Advances 23:41-61, 2005, can benefit from the disclosed route bypassing PAPS and thus requiring one less ATP molecule for sulfate assimilation.

EXAMPLES Example 1 Multiple Methionine Production Pathways, One of which Utilizes Direct Sulfhydrylation, using Exogenously Expressed Nucleic Acid Sequences

A. Construction of a microorganism having both metABC (Transsulfuration) and metAZ (Direct Sulfhydrylation)

As described before, endogenous production of methionine in E. coli occurs mainly through the transulfuration reaction. This Example describes the engineering of E. coli to increase direct sulfhydrylation while also maintaining the endogenous metABC pathway.

Direct sulfhydrylation was increased by cloning O-succinylsulfhydrylase (EC 4.2.99.-) which converts O-succinylhomoserine to homocysteine by reacting with hydrogen sulfide. This enzyme is codified by metZ and can be found in some Pseudomonas species (Vermeij and Kertesz, J Bacteriol. 181:5833-5837, 1999 and Inoue et al., J. Bacteria 179:3956-3962, 1997).

More specifically, metZ from Pseudomonas aeruginosa was cloned into methionine auxotrophs of strain TF4076BJF, which was derived from threonine-producing strain TF4076, (additionally modified by the deletion of thrB and metJ, and the insertion of metF under the control of the pTrc promoter, further described in Example 3, below). These auxotrophs have deletion of either the metB or the metB and metC genes. metZ from Pseudomonas aeruginosa enhanced the growth of the metB and the metBC deletion mutants in minimal medium. Even though in flask cultures methionine production was not fully recovered, metZ expression induces the methionine production up to ˜100 mg/L in metBC deletion mutant, as shown in Table 1. This indicates that metZ is responsible for the production of homocysteine in the cell.

Low methionine production of the deletion mutants transformed with metZ may be due to the limitation of sulfide in the intracellular fraction (methods of increasing sulfide concentration are provided below). This is supported by the finding that the growth of the metBC deletion strain transformed with metZ was enhanced in M9 media in the presence of 2 mM sodium sulfide. In in-vitro assays, the O-succinylsulfhydrylase had low sulfide affinity. Through directed evolution, it is possible to develop improved O-succinylsulfhydrylases with higher sulfide affinity and also higher activity. A highly active O-succinylsulfhydrylase could replace metB and metC in the methionine pathway, or could complement the pathway to increase the carbon flux to methionine.

TABLE 1 Growth complementation and methionine production on TF4076BFJ-ΔBC glucose met intermediate GA and HS used (mg/L) (g/L) TF4076BJF-ΔBC OD (g/L) OSH met HS GA empty vector 2.5 10.0 3867 0.0 0.0 0.4 pCL-metB 20.9 38.1 0.0 0.0 0.6 0.2 pCL-metB-metC 9.7 40.0 0.0 670 4.36 2.4 pPro-metZ 13.0 40.0 0.0 101 3.1 4.3 pCL-metB: metB with its own promoter in pCL1920 pCL-metB-metC: metB and metC with their own promoters in pCL1920 pPro-Z: metZ from Pseudomonas aeruginosa in pProLar vector (ClonTech)

B. Construction of a Microorganism Having Both metABC (Transsulfuration) and metXY (Direct Sulfhydrylation)

This example shows simultaneous methionine production from two pathways in E. coli. One pathway is the endogenous metABC pathway and the second pathway allows for direct sulfhydrylation via the expression of metY and metX from various organisms.

As shown in FIG. 1 E. coli produces methionine endogenously using the transsulfuration pathway genes metA, metB and metC and goes through OSHS. Genetic engineering was used to add an additional pathway to E. coli by cloning and expressing the genes metX and metY into E. coli, which resulted in a host organism that makes methionine through both transsulfuration and direct sulfhydrylation simultaneously.

The metY and metX genes used to construct the heterologous pathway were cloned from Leptospira meyeri, Deinococcus radiodurans, Chloroflexus aurantiacus, Brevibacterium linens, Nostoc punctiforme and Pseudomonas aeruginosa DNA as described below, and several different strains were constructed to analyze the impact of the addition of these genes on methionine production. The homocysteine synthase from Corynebacterium glutamicum and Saccharomyces cerevisiae were also cloned and tested. Both pathways were demonstrated to work simultaneously and methionine production was improved with this addition.

To evaluate whether the L. meyeri metX and metY enzymes could complement the growth of an E. coli methionine auxotroph, the L. meyeri metYX gene cluster was amplified from plasmid metXY-pCR2.0-TOPO and cloned into the pPRO-Nde-del vector. The transcription of the metYX genes in this plasmid was initiated by a lac/ara promoter located on the vector.

Four E. coli strains including W3110 ΔmetA (stopping production of OSHS), TF4076BJF (increased homoserine production), TF4076BJF ΔmetA (stopping production of OSHS), and TF4076BJF ΔmetAmetB (stopping production of OSHS and cystathionine from OAHS or OSHS) were evaluated. Strain TF4076BJF is a threonine auxotroph, deregulated for methionine production with an increase carbon flux up to homoserine, which is able to produce methionine through the natural E. coli pathway.

The strains were transformed with the cloning vector and the plasmid containing metYX, respectively. The transformants were then streaked onto M9 minimal medium plates containing glucose (2 g/L), isoleucine (0.15 g/L), threonine (0.3 g/L), kanamycin (50 mg/L), and IPTG. The metYX gene cluster from Leptospira meyeri complemented the growth of W3110 ΔmetA within 24 hrs. The W3110ΔmetA strain expressing only metX was not able to grow on the M9 minimal plate. Therefore, E. coli W3110 lacks an efficient enzyme to use O-acetyl-L-homoserine as the precursor for methionine biosynthesis. Strain W3110ΔmetA transformed with the control empty vector, pPRO-Nde-del, as described in WO2006113897, did not grow within 48 hrs. Strain TF4076BJF grew on the minimal medium plates when transformed with either the cloning vector or the plasmid containing metYX from L. meyeri.

Alternative metYX genes were also tested for growth complementation in minimal medium. In cloning the metYX genes from D. radiodurans, C. aurantiacus, B. linens, N. punctiforme, the translation of the metX gene was coupled with the translation of the metY gene initiated by a rbs located on the vector, due to the absence of an efficient E. coli ribosomal binding site (rbs) adjacent to the downstream gene, metX.

The metYX gene cluster from L. meyeri, D. radiodurans and C. aurantiacus were the most efficient in complementing the growth of the methionine auxotrophic strains. The complementation of growth was also observed in a methionine auxotroph where metY (L. meyeri) was replaced with the metY (P. aeruginosa) in the L. meyeri metYX gene cluster. These cells showed a reduced growth rate relative to the same methionine auxotroph expressing the L. meyeri metYX.

Methionine production was determined using the shake flask protocol described in Example 3. Briefly, cultures were grown at 30° C. for 50 hours in the medium supplemented with 150 mg/L of methionine (to improve initial growth) and methionine was measured by HPLC. Table 2 shows that the production of methionine was higher in the strains that carried both pathways compared to those where only the transsulfurylation or the direct sulfhydrylation was available.

TABLE 2 Methionine Production Methionine Glucose Produced used (final − initial) Strain OD g/L mg/L TF4076BJF 8.2 40.0 439 TF4076BJF metYX(Lm) 10.2 36.5 984 TF4076BJF metY(Pa)metX(Lm) 9.2 29.1 299 TF4076BJF metYX(Dr) 8.8 40.0 510 TF4076BJF metYX(Ca) 12.1 40.0 740 TF4076BJF ΔmetA metYX(Lm) 5.8 23.6 368 TF4076BJF ΔmetA metY(Pa)metX(Lm) 6.6 21.1 79 TF4076BJF ΔmetAB metYX(Lm) 6.2 23.7 280 TF4076BJF ΔmetAB metYX(Dr) 6.6 32.6 140

Genes metA, and metB are needed for the synthesis of methionine in E. coli strains. When either one of the genes is inactivated, E. coli loses de novo methionine production capability. The data above indicate that the addition of the metYX operon restores methionine production to levels similar to those obtained with a methionine prototroph. Methionine production was in some cases more than double when both pathways are available to the cell. These results demonstrate that the pathways are not mutually exclusive and that homoserine is converted to methionine via both routes.

To further demonstrate the benefits of the dual pathway, the strains were compared in 5 Liter fermentation vessels using the fermentation protocol described in Example 3. Methionine accumulation started after approximately 24 hours and continued until the feed was stopped. The enzyme coded by the metY gene from most organisms is feedback inhibited by high concentrations of methionine. In some cases, the enzyme coded by the metX gene is also feedback inhibited. As a result, significant accumulation of homoserine and OAHS were observed in these fermentations. A comparison of methionine production in fermentors is shown in FIG. 2 and the data are summarized in Table 3. These results confirmed the observation seen in the flasks, that the production of methionine could be enhanced significantly by the adequate expression of a heterologous direct sulfhydrylation pathway, and that this pathway could be responsible for the majority of the methionine production if the enzymes were properly expressed.

TABLE 3 Heterologous expression of direct sulfhydrylation pathway Methionine O-Acetylhomoserine Strain accumulation g/L accumulation (g/L) TF4076BJF 2.1 — TF4076BJF metYX(Lm) 4.7 7.7 TF4076BJF metY(Pa)metX(Lm) 1.5 20.0 TF4076BJF metYX(Dr) 4.7 32.4 TF4076BJF metYX(Ca) 4.9 20.7 TF4076BJF ΔmetA metYX(Lm) 4.1 6.2

To increase the flow of products through to methionine, a metY and a metX that are feedback inhibition resistant can be used. It is also possible to regulate the level of expression of metX and the expression of metH to drive the homoserine faster to methionine.

The differences in methionine production indicate that the metXY pathway is highly effective in E. coli and that the metXY pathway added to a deregulated strain such as this can result in more than double the accumulation of methionine.

Example 2 Homocysteine Synthase that Utilizes Either O-acetyl L-homoserine (OAHS) or O-succinyl L-homoserine (OSHS)

This example describes methods used to isolate a homocysteine synthase encoded by metY from Pseudomonas aeruginosa (ATCC 47085). This enzyme is inhibited by both L-methionine and S-adenosyl L-methionine. The enzyme activity was analyzed according to Yamagata, Methods in Enzymology, 143:478, 1987. The method was slightly modified in that multiple samples points were taken, guanidine was used to quench the reaction and the formation of homocysteine was detected using DTNB ((5,5-Dithiobis(2-nitrobenzoic acid) Sigma D8130) as in the analysis for metA described in Example 3.B. One enzyme unit (U) was defined as the formation of one μmole of homocysteine per minute at room temperature.

MetY from P. aeruginosa was expressed and analyzed using 17.5 μg of purified protein (N-tagged). In contrast to the metY from L. meyeri and to most other published homocysteine synthases, this enzyme was active with both acetyl and succinyl-homoserine. The activity was similar for both substrates, it was feedback inhibited by methionine and SAMe and the level of feed back inhibition seemed to be slightly lower when OSHS was the substrate. Some inhibition was observed at 1 mM methionine. With OAHS as substrate, at 10, 50 and 100 mM the enzyme retained about 50%, 19% and 9%, respectively, of the activity it had in the absence of methionine. The activity in the presence of 5 and 10 mM SAMe was approximately 72% and 21% of the original activity. When OSHS was the substrate the activity dropped to 53% and 31% in the presence of 50 and 100 mM methionine and 86% and 19% in the presence of 5 and 10 mM SAMe.

Example 3 Methods of Genetically Engineering Host Stains to Increase the Production of Methionine

In addition to adding methionine biosynthetic pathways to host organisms as described above in Example 1, the host organism can be further genetically engineered to decrease methionine biosynthetic pathway inhibition, increase reactant availability, and/or decrease product catabolism.

A. Inactivation of Methionine Global Repressor and Threonine Kinase Together with Enhanced Expression of 5,10-methylene-tetrahydrofolate Reductase to Increase Methionine Production.

One method of making a methionine production strain is to modify a strain that has already been engineered to produce an amino acid, such as threonine. For example, the threonine producing strain TF 4076, described in Korean Pat. Publication No. 92-8365 (KFCC 10718) can be used, even though it is a methionine auxotroph). Additional example strains include those deposed in ATCC (13070, 13071, 21148, 21149, 21150, 21151, 21272, 21277, 21278, 21318, 21319, 21320) that are described as threonine overproducers.

Using strain TF 4076 as a starting point, methionine production was enhanced by deleting the thrB gene to avoid threonine production and deleting the metJ gene to release the repression of the expression of the methionine biosynthetic pathway. The strain was also modified to overexpress the metF gene.

thrB Deletion

thrB was deleted using a loxP-chloramphenicol (loxP-Cm) cassette (Gene 2000 vol. 247, p255-264). The thrB gene was cloned by PCR using primer sequences 1 and 2 (SEQ ID NOS: 5 and 6) using the chromosome from E. coli K12 as a template. PCR conditions of 94° C. for 30 seconds; then 25 cycles of 94° C. for 30 seconds, 55° C. for 30 seconds, and 72° C. for 3 minutes; and 72° C. for 7 minutes, with HL PCR premix (Bioneer Co, Korea) were used. PCR products were gel eluted and cloned into the pCR2.1-topo cloning kit (Invitrogen, USA) and named pCR-thrB. pCR-thrB was digested using pflMI and the loxP-Cm cassette was inserted. From this plasmid, the thrB gene containing loxP-Cm cassette was PCR amplified using primers 1 and 2 (SEQ ID NOS: 11 and 12). The PCR products were gel purified. The PCR fragments were electroporated into the TF4076 strain and chloramphenicol resistant colonies were selected and confirmed for thrB deletion. The chloramphenicol marker was removed from an identified colony and the final strain obtained was named TF4076B. This strain did not grow on M9 minimal medium (DIFCO) without threonine, indicating that this strain is a threonine auxotroph.

1. thrB SEQ ID NO: 11 5′- GCT AGC c atg gtt aaa gtt tat gcc  ccg -3′ 2. thrB SEQ ID NO: 12 5′- GAG CTC tta gtt ttc cag tac tcg tgc  gc -3′ metJ Deletion

To delete the methionine global repressor metJ gene, the FRT one step deletion method was used (Datsenko and Wanner PNAS 97:6640-6645, 2000). PCR fragments were amplified using primer sequences 3, 4 (SEQ ID NOS: 13 and 14) and template pKD3 (see, Datsenko and Wanner, PNAS 97:6640-6645, 2000). The PCR conditions used were 94° C. for 30 seconds; followed by 25 cycles of 94° C. for 30 seconds, 55° C. for 30 seconds, and 72° C. for 1 minute; then 72° C. for 7 minutes, with HL PCR premix (Bioneer Co., Korea). Chloramphenicol resistant colonies were selected and the metJ gene deletion was confirmed using PCR primer sequences 5 and 6 (SEQ ID NOS: 15 and 16). Using pCP20 plasmid transformation, the chloramphenicol marker gene was removed and the removal was confirmed using PCR. The strain obtained was named as TF4076BJ.

3. metJ + chloramphenicol SEQ ID NO: 13 5′-atggctgaat ggagcggcga atatatcagc ccatacgctg agcacggcaa ggtgtaggct ggagctgctt c-3′ 4. metJ + chloramphenicol SEQ ID NO: 14 5′-gtattcccac gtctccgggt taatccccat ctcacgcatg atctccatat gaatatcctc cttag-3′ 5. metJ SEQ ID NO: 15 5′-gggctttgtc ggtgaaatg-3′ 6. metJ SEQ ID NO: 16 5′-actttgcgat gagcgagag-3′ metF Integration

To complement the methionine auxotrophy of TF4076BJ, the metF gene was expressed in strain TF4076BJ. The metF gene was amplified using primer sequences 7 and 8 (SEQ ID NOS: 17 and 18) and the chromosome of E. coli K12 strain as the template. PCR conditions of 94° C. 30 seconds, then 25 cycles of 94° C. 30 seconds, 55° C. 30 seconds, 72° C. 1 minute, and then 72° C. 7 minutes and HL PCR premix (Bioneer Co., Korea) were used. PCR fragments were gel eluted and inserted into the NheI and Sad sites in the pSE380 vector (Invitrogen Co.). The plasmid was named pSE380-metF. pSE380-metF was transformed into the TF4076BJ strain. The transformant grew on M9 minimal medium (Difco) containing threonine and isoleucine indicating the complementing of methionine auxotrophy.

The expression level of the metF gene under the control of two different promoters was determined. The promoters were the pCJ1 promoter (PCT/KR2005/004338) and the pThreonine promoter. The metF gene was amplified using primer sequences 9 and 10 (SEQ ID NOS: 19 and 20) and the chromosome of Escherichia coli K12 strain as the template. PCR conditions of 94° C. 30 seconds, then 25 cycles of 94° C. 30 sec, 55° C. 30 sec, 72° C. 1 min, and then 72° C. 7min and HL PCR premix (Bioneer Co., Korea) were used. PCR fragments were gel eluted and ligated into the PvuII and HindIII sites in the pCL1920 vector (Lerner and Inouye, Nucleic acids Research 18:4631, 1990) containing the pCJ1 promoter or the pThreonine promoter. The pCJ1 promoter was PCR amplified using primer sequences 11 and 12 (SEQ ID NOS: 21 and 22) and the pThreonine promoter was amplified from the E. coli K12 chromosome using primer sequences 13 and 14 (SEQ ID NOS: 23 and 24). The PCR fragments were gel eluted and integrated into the KpnI and EcoRV sites in the pCL1920 vector. The PCR conditions used were the same as above. The plasmid containing the metF gene under the control of the pCJ1 promoter was named pCL-pCJ1-metF and the plasmid containing the metF gene under the control of the pThreonine promoter was named pCL-pThr-metF. Each plasmid was transformed to TF4076BJ strain and methionine production was measured.

A shake flask culture protocol was used to test the strains as follows: a seed culture was incubated at 31° C. for 6 hrs in medium consisting of (in 1 L): 10 g Yeast extract, 6 g Na₂HPO₄.12H₂O, 0.5 g NaCl, 3 g KH₂PO₄, 2 g glucose, 0.49 g MgSO₄.7H2O, 0.015 g CaCl₂.2H₂O. It was then used to inoculate flasks with the following medium: (1 L): 17 g (NH₄)2SO₄, 1 g MgSO₄.7H2O, 2 g Yeast extract, 0.3 g L-threonine, 10 mg MnSO₄.7H₂O, 10 mg FeSO₄.7H₂O, 10 mg Zn SO₄, 30 g CaCO₃, 40 g glucose, and 2 g KH₂PO₄ pH 7.2. The flasks were incubated for 64 to 72 hours at 31° C. with shaking at 250 rpm. After centrifugation, culture supernatant was isolated and used for methionine analysis.

For the culture of cells containing the pSE380-metF plasmid, 100 μg/L ampicillin and 0.5 mM IPTG was added in the media. The metF gene under the control of the pCJ1 promoter produced the most methionine as shown in Table 4.

TABLE 4 Methionine production in cells containing various metF expression cassettes glucose used OD (g/L) Methionine (mg/L) TF4076BJ 7.8 34 0 TF4076BJ/pSE380-metF 5.4 29 130 TF4076BJ/pCL-pCJ1-MetF 7.4 35 206 TF4076BJ/pCL-pthr-MetF 22 40 136

To express the metF gene more stably, metF genes under pTrc, pCJ1, and pThreonine promoters were integrated into the lacZ locus of the TF4076BJ chromosome. Each metF gene was PCR amplified from each plasmid and inserted into the NsiI site in the pBrint vector (Borgne et al., Gene 223:213-219, 1998). The vectors were transformed into the TF4076BJ strain and a transformant that grew on media containing chloramphenicol at 37° C. was selected and confirmed for metF gene integration into the LacZ locus of the chromosome. Selected colonies were transformed by pJW168 and the chloramphenicol marker was deleted. The cells containing pCJ1-metF gene could not be obtained and the transformant containing pThr-metF cassette did not grow well. Only the cells containing pTrc-metF gene in the LacZ locus grew well. The flask culture of this strain showed ˜600 mg/L methionine production in the presence of 0.5 mM IPTG in the media. The final strain containing pTrc-metF gene was named as TF4076BJF and was further analyzed.

In summary, the TF4076BJF strain was derived from threonine-producing strain TF 4076, which was modified by the deletion of thrB and metJ, and the insertion of metF under the control of the pTrc promoter. Table 5 shows the production of homoserine and methionine by TF4076BJF.

TABLE 5 Methionine production of the strain TF4076BJF Glucose used Homoserine Methionine Strain OD (g/L) production (g/L) production (g/L) TF4076BJ 15.3 24.7 0.62 0 TF4076BJF 10.6 34.7 4.2 0.64

7. metF SEQ ID NO: 17 5′- GCT AGC c atgagcttttttcacgccag -3′ 8. metF SEQ ID NO: 18 5′- GAG CTC ttataaaccaggtcgaaccc -3′ 9. metF SEQ ID NO: 19 5′- CAGCTGatgagcttttttcacgccag- 3′ 10. metF SEQ ID NO: 20 5′- AAGCTT ttataaaccaggtcgaaccc- 3′ 11. CJ1 promoter SEQ ID NO: 21 5′- cgg ggt acc acc gcg ggc tta ttc cat tac  at- 3′ 12. CJ1 promoter SEQ ID NO: 22 5′- acg cga tat ctt aat ctc cta gat tgg gtt  tc- 3′ 13. threonine promoter SEQ ID NO: 23 5′- cgg ggt acc tgg tta caa caa cgc ctg g- 3′ 14. threonine promoter SEQ ID NO: 24 5′- cat gat atc tac ctcg tta cc ttt ggt cg-  3′

Strain TF4076BJF was grown in 5 L fermentors according to the protocol described below, and a production of approximately 2.2 g/L of methionine was obtained in 96 hrs.

5 L fermentations were performed using the following protocol. To compare the effect of the different genes cloned in the E. coli strain, a basic fermentation protocol for 5 Liter jars was used. The inoculum was grown in 25 mL of medium consisting of 10.0 g yeast extract, 4.49 g Na₂HPO₄.7H₂0, 0.5 g NaCl, 3.0 g KH₂PO₄, 0.49 g MgSO₄.7H₂O, 0.015 g CaCl₂.2H₂O, and 2 g/L glucose in 1 L volume. 50 mg/L of the appropriate antibiotic was used depending on the resistance of the strain being tested. After incubation with shaking at 31° C. and 250 rpm for 8-24 hours, the culture was transferred to 200 mL of the same medium and incubated under the same conditions for 16 to 20 hours. This culture was used to inoculate fermentors with 2.5 L of medium.

The fermentation medium consisted of: 17.0 g/L (NH₄)₂SO₄, 2.0 g/L yeast extract, 2.0 g/L KH₂PO₄, 1.0 g/L L-threonine, 0.3 g/L isoleucine, 0.01 g/L MnSO₄-H₂O, 0.01 g/L FeSO₄-7H₂O, 0.01 g/L ZnSO₄-7H₂O, 1.0 g/L MgSO₄-7H₂O, 2 mg/L piridoxal, 2 mg/L vitamin B12 and 40 g/L glucose. Antibiotics and IPTG were added depending on the strain being grown. The fermentation temperature was maintained at 31° C., the dissolved oxygen above 30% of saturation and the pH was initially controlled with 28% NH₄OH. After the glucose was exhausted, the pH would rise. At that point, a continuous fixed feed would be started, or 100-150 mL aliquots of feed would be added at a time, based on increases in pH. The feed consisted of 4.0 g/L yeast extract, 33 g/L (NH₄)₂SO₄, 3.0 g/L KH₂PO₄, 1.5 g/L L-threonine, 1.0 g/LMgSO₄-7H₂O, 2 mg/L vitamin B 12 and 400 g/L glucose. Some minor variations to the medium and feed were introduced depending on the strain. The fermentation proceeded for a total of 72 to 96 hours. Methionine concentration was measured throughout, as well as cell growth by optical density and glucose utilization.

B. Generation of Feedback-Resistant Homoserine Succinyltransferases for Methionine Production

An E. coli strain was constructed with the metA and the metB genes deleted. This strain showed homoserine accumulation due to the loss of MetA activity. When the wild-type metA cassette was expressed in this strain, OSHS was produced by MetA activity in the absence of methionine. However, when methionine was added in the media, the strain with wt-metA cassette accumulated homoserine again due to the feedback inhibition of MetA activity. Thus, feed back resistant metA genes can be identified by testing for O-succinyl homoserine accumulation in the presence of methionine. The mutant producing more OSHS in the presence of high amount of methionine in the media contains the most feed-back inhibition resistant metA.

A schematic representation of the screening methodology is provided in FIG. 3.

Construction of metB Deletion Mutant

To make a metB deletion mutant in TF4076BJF, the FRT one step deletion method was used (Datsanko and Wanner, PNAS 97:6640-6645, 2000). PCR fragments were amplified using primer sequences 15 and 16 (SEQ ID NOS: 25 and 26) and template pKD3 was electroporated into TF4073BJF cells. The PCR conditions of 94° C. 30 seconds, 25 cycles of 94° C. 30 seconds, 55° C. 30 seconds, 72° C. 1 minutes, then 72° C. 7min and HL PCR premix (Korea, Bioneer Co) were used. Chloramphenicol resistant colonies were selected and confirmed for metB gene deletion using PCR. The chloramphenicol marker gene was removed using pCP20 plasmid transformation, and the removal was confirmed by PCR. The strain obtained by this procedure was named as TF4076BJF-B.

15. metB + chloramphenicol SEQ ID NO: 25 5′-TTACTCTGGT GCCTGACATT TCACCGACA AAGCCCAGGG AACTTCATCA Cgtgtaggct ggagctgctt c -3′ 16. metB + chloramphenicol SEQ ID NO: 26 5′-TTACCCCTTG TTTGCAGCCC GGAAGCCATT TTCCAGGTCG GCAATTAAA Tcatatgaat atcctcctta g -3′ Construction of metA Deletion Mutant

To make a metA deletion mutant in TF4076BJF-B, the FRT one step deletion method was used (PNAS .97:6640-6645, 2000). PCR fragments were amplified using primer sequences 17, 18 (SEQ ID NOS: 27 and 28) and template pKD3 was electroporated into TF4073BJF-B cells. The PCR conditions of 94° C. 30 seconds, 25 cycles of 94° C. 30 seconds, 55° C. 30 seconds, 72° C. 1 minute, then 72° C. 7 minutes and HL PCR premix (Korea, Bioneer Co) were used. Chloramphenicol-resistant colonies were selected and confirmed for metA gene deletion using PCR. The chloramphenicol marker gene was removed using pCP20 plasmid transformation, and the removal was confirmed by PCR. The strain obtained by this procedure was named as TF4076BJF-BA.

17. metA + chloramphenicol SEQ ID NO: 27 5′- CAATTTCTTGCGTGAAGAAAACGTCTTTGTGATGACAACTT CTCGTGCGTgtgtaggctggagctgcttcc -3′ 18. metA + chloramphenicol SEQ ID NO: 28 5′- AATCCAGCGTTGGATTCATGTGCCGTAGATCGTATGGCGTG ATCTGGTAGcatatgaatatcctccttag-3′ Construction of metA Expression Vector

To make a metA library, a metA expression vector was constructed. The metA gene was amplified using primer sequences 19 and 20 (SEQ ID NOS: 29 and 30) with the chromosome from the E. coli K12 strain as the template. The PCR conditions of 94° C. 30 seconds, 25 cycles of 94° C. 30 seconds, 55° C. 30 seconds, 72° C. 1 minute, then 72° C. 7 minutes and HL PCR premix (Korea, Bioneer Co) were used. The PCR fragments were gel eluted and ligated into pCL1920 at the SmaI site. The plasmid was named pA-CL. The pA-CL plasmid was transformed into the TF4076BJF-AB strain and flask culture was performed with and without methionine. OSHS and homoserine were measured by the same method as described above for methionine. As shown in Table 6, the cells containing the pA-CL plasmid in the absence of methionine produced 3.8 g/L OSHS with 0.24 g/L homoserine. However, in the presence of 1 g/L methionine the cells produced 5.8 g/L OSHS with 4.9 g/L homoserine. The increase of OSHS amount is due to the increase of growth by methionine addition, while the increase of homoserine is due to the feed-back inhibition of metA activity by methionine.

TABLE 6 O-succinyl homoserine and homoserine production in TF4076BJF-AB strain containing pA-CL plasmid Glucose OSH HS Methionine used production production addition Strain OD (g/L) (g/L) (g/L) 0 g/L TF4076BJF-AB /pC11920 2.2 14.2 0 1.42 0 g/L TF4076BJF-AB /pA-CL 2.1 13.1 3.8 0.24 1 g/L TF4076BJF-AB /pC11920 4.7 39.8 0 5.7 1 g/L TF4076BJF-AB /pA-CL 6.4 37.4 5.9 4.9

19: metA SEQ ID NO: 29 5′-aatggatccTGCCGTGAGCGGCGAATAC-3′ 20: metA SEQ ID NO: 30 5′-agctctagaCTGCTGAGGTACGTTTCGG-3′ Construction of pA-CL Mutant Library

To make a pA-CL mutant library, error-prone PCR was performed. Error-prone PCR was done using the primer sequences 21 and 22 (SEQ ID NOS: 31 and 32) with the pA-CL plasmid as a template. The PCR conditions of 94° C. 30 seconds, 25 cycles of 94° C. 30 seconds, 55° C. 30 seconds, 68° C. 2 minutes, then 72° C. for 7 minutes and BD diversify PCR mutagenesis kit (BD, USA) were used. PCR fragments were digested by BamHI and XbaI and ligated into pCL1920. The library was transformed into strain TF4076BJF-AB and ˜30,000 transformants were collected for further analysis.

21: pCL1920 SEQ ID NO: 31 5′-CGAAGTAATCGCAACATCCG-3′ 22: pCL1920 SEQ ID NO: 32 5′-GTCTGCTATGTGGTGCTATC-3′ Preparation of MetB Enzyme Crude Extract

To measure the OSHS by enzymatic method, the MetB enzyme from E. coli was used. The MetB enzyme reacts with OSHS and cysteine in a 1:1 ratio and produces cystathionine. The reagent DTNB (5,5-Dithiobis(2-nitrobenzoic acid) Sigma D8130) reacts with the free SH group of cysteine and makes a yellow color which can be measured at 415 nm. Before the MetB reaction, cysteine reacts with DTNB and turns to yellow color. After the MetB reaction, cysteine turns to cystathionine which can not bind to DTNB. By the decrease of OD at 415 nm after the reaction, the amount of OSHS in the reaction mix can be measured.

For the overexpression of MetB enzyme, the PCR amplified metB gene from E. coli K12 chromosome was digested by BamHI and HindIII and cloned into the pCDF-Duet vector (Novagene, USA). A PCR reaction was performed using the primer sequences 23 and 24 (SEQ ID NOS: 33 and 34) and the E. coli K12 chromosome as the template. The PCR conditions of 94° C. 30 seconds, 25 cycles of 94° C. 30 seconds, 55° C. 30 seconds, 72° C. 1 minute, then 72° C. 7 minutes and HL premix (Bioneer, Korea) were used. The plasmid containing the metB gene was transformed into E. coli using a Tuner cell (Novagen, USA) and the transformant was grown overnight with LB media containing 50 μg/mL spectinomycin. The overnight culture broth was diluted in LB media containing 50 μg/mL spectinomycin and incubated at 37° C. until it reached an OD at 600 nm of 0.6, at which point IPTG was added to a final concentration of 0.2 mM and the culture was incubated for 4 hrs at 30° C. The cells were harvested by centrifugation at 12,000 rpm, resuspended in 0.1 M potassium phosphate buffer (pH 7.5) and ruptured by sonication (5×30 seconds). Crude cell extract was acquired by centrifugation for 20 min at 12,000 rpm and the supernatant was then used for enzyme assay.

23: metB SEQ ID NO: 33 5′-gccaggatccgATGACGCGTAAACAGGCCAC-3′ 24: metB SEQ ID NO: 34 5′-ccgcaagatTTTACCCCTTGTTTGCAGCC-3′ Screening of Feed Back Resistant metA

Feedback resistant metA mutations were identified by inoculating the TF4076BJF-AB strain containing pA-CL mutants into 96 well plates containing microfermentation media and culturing for 48 hrs at 31° C. with shaking. Microfermentation media is 1 volume of shake flask media as described in Example 3, and 1 volume of 0.05M potassium phosphate buffer pH 6.5, with 5 g/L L-methionine.

The 96 well plates were then centrifuged for 10 min at 3,000 rpm and OSHS was measured in the supernatant by the enzymatic method described above (Preparation of MetB crude extract). 50 μL of the culture supernatant was mixed with 50 μL of reaction buffer (Reaction buffer: 0.1 M potassium phosphate buffer (pH 7.5)+2.5 mM cysteine+1/500 10 mM PLP (pyridoxal 5′-phosphate hydrate, Sigma P9255)+1/100 MetB crude extract (5 mg/mL)). The reaction was incubated for 10 minutes at 37° C. 100 μL DTNB (4 mg/10 mL 0.1 M potassium phosphate buffer, pH 7.5) was added and the OD at 415 nm was taken. 1 or 2 colonies showing the lowest absorbance at 415 nm were selected from each 96 well plate and they were streaked onto LB media containing 50 μg/mL spectinomycin. The resulting colonies were inoculated onto another 96 well plate containing microfermentation media and a second round of screening was performed. The selected strains were then tested under the shake flask culture conditions described above, with the addition of 5 g/L methionine to the medium, and O-succinylhomoserine production was measured.

24 mutants from 12, 000 colonies were selected for flask culture and 14 mutants were selected for sequencing. From those, 5 new mutants were identified. The other remaining 9 mutants possessed the same mutations as had been previously reported. The accumulation of O-SHS and homoserine in shake flask culture for the 14 mutants is shown in Table 7, and the amino acid changes in the metA sequences of the selected mutants are shown in Table 8.

TABLE 7 Shake flask performance of selected mutants OSH HS Glucose production production Strain No OD used (g/L) (g/L) (g/L) Control (TF4076BJF-AB/pA-Cl) 6.0 40 4.9 5.5 #7 4.9 40 9.2 2.9 #8 4.6 40 5.4 3.8 #10 4.7 40 8.8 3.0 #11 4.7 40 9.1 2.8 #32 5.8 40 10.7 1.6 #34 5.6 40 10.1 2.4 #36 5.6 40 10.4 2.2 #37 5.9 40 9.6 1.6 #39 7.0 40 9.2 1.0 #22 4.8 40 9.4 1.4 #23 4.6 40 9.6 1.4 #41 5.6 40 11.8 2.1 #43 6.1 40 11.2 2.3 #47 6.0 40 11.2 2.2 #49 5.6 40 11.5 2.1

TABLE 8 Sequence analysis of selected mutants 32 37 10 11 41 SEQ ID SEQ ID SEQ ID SEQ ID SEQ ID NO: position wt NO: 2 NO: 4 NO: 6 NO: 8 10  24 T S (A70T)  29 S P (T85C)  79 N S (A236G) 114 E G (A341G) 140 F S (T419C) I (T418A) 163 K Q (A487C) 222 F L (T666A) 275 A E (C824A) 290 N H (A868C) 291 Y N (T871A) 295 Q R (A884G) 297 T A (A889G) 304 M L (A910T) 305 N Y (A913T) no amino A105G, C222T T450C T915C T573C acid A597T change Feed Back Resistance of Mutant metA

Since all the feed-back inhibition resistant metAs produced similar amounts of OSHS in the presence of 5 g/L methionine in the flask culture, higher concentrations of methionine were added in the flask culture media and the production of OSHS was determined. After 64 hrs of culture with 30 g/L L-methionine, production of OSHS decreased only in the #37 mutant sample, and all the others showed similar levels of OSHS production as in the presence of 5 g/L methionine. These results, presented in Table 9, indicated that the feed-back inhibition resistance metAs were resistant to concentrations as high as 30 g/L methionine.

TABLE 9 OSHS production of mutant metAs in the presence of 30 g/L methionine OSH HS Glucose production production Strain OD used (g/L) (g/L) (g/L) Control (TF4076BJF-AB/pA-Cl) 4.36 38.6 2.7 1.1 #10 3.3 33.1 10.6 0.44 #11 3.5 36.6 11.5 0.22 #32 3.1 30.2 10.7 0.23 #37 2.0 22.0 6.2 0.05 #41 4.4 40.0 10.5 Not analyzed In-vitro Characterization of Mutant metA Proteins

PCR was used to amplify and then clone the five metA mutant genes identified as pCL-A#10, pCL-A#11, pCL-A#32, pCL-A#37, and pCL-A#41, into the pET30a vector. All constructs were subjected to DNA sequence analysis to confirm the presence of mutations. The genes were cloned with a C-terminus His tag for enzyme purification. The enzymes were overexpressed, purified and the activity was measured in the presence of different levels of methionine and SAMe, as described by Lawrence, J. Bacteriol., 109:8-11, 1972. The only modifications to the assay were that multiple points were taken and that the reaction was quenched with guanidine. Table 10 provides a summary of the activity from the various mutants, and clearly shows that all the mutants were feed-back inhibition resistant when compared to the wild type enzyme and that mutants #10 and #11 were the most resistant to both methionine and SAM inhibition.

TABLE 10 Characterization of mutant and wild type MetA enzymes #10 #11 #32 #37 #41 Specific activity SEQ ID SEQ ID SEQ ID SEQ ID SEQ ID (U/mg)* w.t. NO: 6 NO: 8 NO: 2 NO: 4 NO: 10 control 386  176 479 276 228 315 w/ 100 mM Met 29 172 451 218 190 232 w/ 300 mM Met — 125 282 — — — w/10 mM SAM 11 150 395 78  63 108 % of specific activity retention w.t. #10 #11 #32 #37 #41 control 100 100 100 100  100  100  w/ 100 mM Met 7.6 97 94 79 83 74 w/ 300 mM Met — 70 56 — — — w/10 mM SAM 2.9 85 82 28 27 34 *Where U is the formation of 1 μmole of CoA per minute at room temperature

Mutants metA#10 and metA#11 (SEQ ID NOS: 5 and 7, respectively) were selected for further analysis. metA mutants #10 and #11 were analyzed for their lack of inhibition in an experiment using 300 mM of methionine. This is close to the highest concentration achievable in the assay conditions. The solubility of methionine in water is 5.6 g/100 mL at 30° C., which corresponds to a concentration of 375 mM. In the presence of 300 mM of methionine, mutant metA#10 retained 70% of its specific activity, and mutant metA #11 retained 55% of its specific activity. Thus, the metA#10 and #11 mutants can be used to in a methionine producing microorganism.

Methionine Production with Feedback Inhibition Resistant metA

metA#10 and metA#11 were individually cloned into the methionine producing strain TF4076BJF. MetA#10 was also cloned together with metYX from L. meyeri. The clones were tested following the fermentation protocol described in Example 3A. Methionine concentrations were assessed after 78 hours of fermentation and the results are shown in Table 11. There was no O-succinylhomoserine accumulation in any of the fermentations. The time courses of methionine production are shown in FIG. 4.

TABLE 11 Methionine Accumulation Strain Final methionine titer (g/L) TF4076BJF 2.1 TF4076BJF metA#10 6.3 TF4076BJF metA#11 4.5 TF4076BJF metA#10 + metYX (Lm) 6.6

These results show that expression of feedback inhibition resistant metAs increased methionine production and that the combination of a direct sulfhydrylation pathway and a feedback inhibition resistant metABC pathway showed less synergy than observed with the native MetA. The less synergy observed indicates that the accumulation of methionine may be inhibiting MetY. To increase methionine production further, a feedback inhibition resistant MetY can be used.

C. Strategies for Attenuation of MetK Activity in E. coli

As described above, the formation of SAMe decreases the concentration of methionine and reduces the activity of the methionine biosynthetic pathway via feed back inhibition of metA.

Isolation of mutants in the metK gene are facilitated by the observation that some ethionine-resistant mutants have reduced levels of metK and overproduce methionine. Table 12, lists various metK mutations that have been described as causing a decrease in MetK activity. These mutants were constructed as described below.

The metK gene from E. coli (Accession number AP_(—)003499 or BAE77005) was cloned and overexpressed with either an N-terminal or a C-terminal His tag in pET28b vector. Site directed mutagenesis was performed using the C-terminal His tagged metK clone to generate the desired mutants. Expression of the mutant MetK proteins was confirmed.

The MetK mutants were purified (using the C-terminal His tag) and assayed in vitro. The wild type C-terminal His-tagged MetK protein was used as a control. The mutants were assayed using a radioactive assay. The assay conditions were as follows:

-   -   Assay Mix:     -   1.0 mL 0.5 M HEPES/KOH, pH 8.0     -   0.5 mL 1.0 M KCl     -   0.2 mL 1.0 M MgCl₂     -   1.0 mL 100 mM ATP (disodium salt, pH 8.0 with KOH)     -   0.1 mL 50 mM methionine     -   0.1 mL NEN [methyl-¹⁴C]methionine     -   6.6 mL H₂O     -   25 mM EDTA pH 8.0 stop for assays.

45 μl of assay mix was added to an Eppendorf tube and 5 μL of enzyme (normalized data shown in Table 13. The reaction was incubated at room temperature (or 25° C.) for a desired period (1 to 10 minutes). The reaction was stopped with the addition of 150 μL of 25 mM EDTA. 100 μL of the reaction was spotted onto a 2.5 cm diameter Whatman P-81 phosphocellulose filter circle (labeled in pencil). The filters were washed with 3 L of distilled water, air-dried and placed in scintillation vials with aquasol. The emissions were counted using a window that extends from ¹⁴C to about 0. Assay efficiency and quench levels were determined by adding a known amount of counts of pure ¹⁴C-SAM and processing through the whole procedure. Backgrounds are typically<100 cpm (total counts ca. 10⁵ cpm per reaction).

TABLE 12 Normalized Activity Activity (CPM Expected Effect SAMe/ μg purified Residue Position Replacement on SAMe synth Reference protein/min) ** His 14 Asn Activity reduced ~ 104 J. Biol 7.7 fold Chem 2000 Asp 16 Asn kcat reduction of ~ 103 J. Biol 2.5 fold Chem 1999 Gly 77 Val Expected Markham 6.9 decrease in personal MetK activity communication Cys 90 Ala Only 10% of WT J. Biol Same as WT activity Chem 1995 Cys 90 Ser Only 10% of WT J. Biol 23.2 activity Chem 1995 Asp 118 Asn kcat reduction of ~ 103 J. Biol 1.3 fold Chem 1999 Val 185 Glu 6.4X increase in AEM 2005 4.9 excreted Met over control Asp 238 Asn kcat reduction of ~ 103 J. Biol 1.9 fold Chem 1999 Cys 239/2 Ala* Only 10% of WT J. Biol Same as WT 40 activity Chem 1995 Lys 245 Met 42,000 fold J. Biol 2.5 lower activity Chem 2000 than WT Asp 271 Ala kcat reduction of ~ 103 J. Biol 0.4 (not duplicated) fold Chem 1999 WT None Cargill 995.4 control * BioTDC WT Untagged None Markham 5600 lab * WT control MetK protein was also C-terminal His tagged for comparison with the tagged mutant metK proteins. An approximately 6-fold decrease in activity was observed with the tagged WT MetK protein when compared to untagged MetK protein activity. **activity for 5 minute reaction time reported

The product of the MetK reaction, SAMe, is a non-competitive inhibitor of MetK. Therefore, reaction kinetics are complicated to analyze and it is expected that the difference between the activities of the wild type and the mutants is even higher. By understanding the activity of the various mutant MetK enzymes a suitable production host can be designed.

D. SAMe Transporter Regulation

S-AdenosylMet (SAMe) serves as the primary methyl group donor in all organisms, is involved in polyamine biosynthesis and is essential for cell growth. S-adenosyltransferase (MetK, EC 2.5.1.6) catalyzes the only known route for SAMe biosynthesis in E. coli, as this organism cannot uptake SAMe from the growth medium. An alternative to the down regulation of metK as described above is to provide E. coli with the ability to uptake SAMe and simultaneously knock-out the metK gene, to reduce or avoid utilization of methionine via that route. Cell growth can then be controlled by the addition of SAMe to the fermentation medium.

A Rickettsia high-affinity SAMe transport system has been identified (Tucker et al., J. Bact. 185: 3031-3035, 2003). This SAMe transporter has K_(T) values of 2-8 μM which is comparable to the values for the transporter from S. cerevisiae (3.3 μM), P. carnii (4.5 μM), and rat liver (8.9 μM). In addition it has been reported that the Rickettsia SAMe transport system can complement an E. coli metK deletion mutant (Driskell et al., J. Bact. 187:5719-5722, 2005).

The strains W3110 and TF4076BJF were transformed with a plasmid containing the SAM transporter mentioned above. The metK gene from W3110 was knocked-out and verified by PCR. According to these modifications, the new strain should have been able to grow only in the presence of SAM, but not without it. However, it continued to grow in both absence and presence of exogenous SAM.

E. Knock Out of Methionine Uptake Transporters to Increase Methionine in Fermentation Medium

Two L-methionine transporters have been, identified in E. coli, one with a very high affinity (Km=0.1-0.13 μM) and a second with lower affinity (Km=20-40 μM). The locus for the high affinity transporter system is designated metD since the metD mutants are unable to transport D-methionine and to utilize it as a methionine source. The metD locus corresponds to the abc (metN), yaeE(metI) and yaeC (metQ) genes which encode an ABC transporter necessary for L-methionine and D-methionine uptake. metN encodes the putative ATPase and metI encodes the membrane-spanning region of the metD ABC transporter. It is expected that the third component, metQ, encodes the substrate-binding domain. Since, metI, metN and metQ deletion mutants can still grow in the presence of L-methionine, it is taken to be indirect evidence for the presence of the low affinity metP system.

As illustrated in FIG. 5, metD imports D- and L-methionine, while the genetically uncharacterized transporter metP imports only L-methionine. MetD is represented as a typical ABC transporter with its three components: A, E, and C represent abc (ATPase), yaeE (permease), and yaeC (D-methionine-binding protein), respectively. (Merlin et al., J. Bacteriol. 184: 5513-5517, 2002).

metJ, the global methionine repressor protein, was shown to negatively control expression of the operon encoding the metD locus. Transcription of the metD genes increases upon deprivation of methionine, which is a metJ corepressor. In cells with a metJ deletion, the transporters are more highly expressed and not repressed by methionine (Merlin et al., J. Bacteriol. 184: 5513-5517, 2002). Methionine productions strains generally have attenuated metJ sequences or med deletions so, to increase production, it can be particularly important to reduce the methionine import activity. The strains can be modified by knocking out the metD methionine uptake system. This will prevent methionine uptake and avoid the potential energy-wasting futile cycle of uptake/excretion.

Knocking out metD resulted in a 25% increase in methionine accumulation in the fermentation broth, as measured by the shake flask protocol described in Example 3, above.

F. Over Expression of metH

The increase in carbon flux through the methionine pathway due to the modifications to the strains described here, can lead to an accumulation of homocysteine inside the cell. Homocysteine is very toxic to the cell. To avoid any accumulation and convert the homocysteine to methionine, it is very important to have very active homocysteine methylase activity (EC 2.1.1.13 and 2.1.1.14) which are codified by the metE and metH, respectively. One way to accomplish this is to overexpress these genes either in a plasmid system or by placing the chromosomal copy under the control of a strong promoter.

The native metH gene from E. coli was overexpressed under several different promoters in a strain containing the dual pathways metABC and metXY, and the methionine production was measured in our standard shake flask protocol. The three vectors used for metH overexpression were pCL-P(cysK), pCL-P(pro), and pCL-P(CJ-1) which were respectively modified from commercially available plasmid pCL1920 by replacing the Plac promoter with the promoter of E. coli cysK gene, the promoter from commercial vector pPROLar, and CJ Corporation's proprietary promoter CJ1. The ORF of the E. coli metH gene was located just downstream of the promoters. The results obtained are shown in Table 13, below. It was clear that even at the relatively low levels of methionine accumulated in the shake flask protocol, the presence of a high concentration of the homocysteine methylase had a very significant positive effect on the production of methionine. The effect was even more pronounced in fermentors.

TABLE 13 Effect of over-expression of metH on methionine production Glucose Methionine used Produced Strains OD g/L mg/L TF4076BJF met YX Lm 7.4 40.0 868 TF4076BJF met YX Lm pcL-P (cysK) met H 11.7 33.9 1289 TF4076BJF met YX Lm pcL-P (pro) met H 7.5 32.8 1062 TF4076BJF met YX Lm pcL-P (CJ-1) met H 12.4 40.0 1337 TF4076BJF met YX Dr 10 38.2 569 TF4076BJF met YX Dr pcL-P (cysK) met H 15.4 40.0 896 TF4076BJF met YX Dr pcL-P (pro) met H 12.5 40.0 786 TF4076BJF met YX Dr pcL-P (CJ-1) met H 15 40.0 856

G. Improving Sulfate Uptake and Increasing APS Pool in Methionine Producing Organisms

This Example describes a method of engineering E. coli to bypass the intermediate, PAPS, in its endogenous sulfur assimilation pathway. The new pathway created requires one less molecule of ATP for each sulfate molecule reduced to sulfide, thus, it is more energy efficient (see, FIG. 6).

As previously described, FIG. 6 shows two ways to take advantage of alternative sulfur assimilation pathways. One way is to clone the adenylyl sulfate reductase, cysH (EC 1.8.4.9) gene from Bacillus or P. aeruginosa and either incorporate it into the E. coli genome or express it from a plasmid. This allows APS to be converted to sulfite in a single step, thus avoiding the conversion of APS to PAPS catalyzed by E. coli APS kinase (cysC). The second way would be to mutate the E. coli PAPS reductase gene, based on the bacterial cysH homologs, so that its substrate specificity is changed from PAPS to APS.

The cysH genes from Bacillus subtilis 168 (Accession number AJ000974 REGION: 548 . . . 1249) and Pseudomonas aeruginosa PA01 (Accession number NC_(—)002516 REGION: 1895692 . . . 1896495) were cloned into plasmids and tested to determine if they could complement E. coli cysC or cysH knockout mutants, which are auxotrophic for both cysteine and methionine.

Briefly, the cysH genes from Bacillus subtilis 168 and Pseudomonas aeruginosa PA01 were transformed into BL21(DE3)ΔcysH, a cysH knockout of BL21(DE3), to test for complementation. Single colonies from the following four strains were used to inoculate 5 mL cultures containing the Overnight Express medium (OnEX: defined medium supplemented with amino acids but not cysteine or methionine) from Novagen.

Cultures were incubated for 48 hrs at 30° C. with constant shaking. The results, presented in Table 14, indicate that both the cysH gene from B. subtilis and P. aeruginosa were able to complement the cysH knockout in E. coli and to sustain growth.

TABLE 14 Optical density at 600 nm of ΔcysH complementation experiments Strain OD₆₀₀ BL21(DE3) (wild type strain) 5.2 BL21(DE3)ΔcysH (with deletion of cysH) 0 BL21(DE3)ΔcysH + pET23BscysH (addition of Bacillus cysH) 7.2 BL21(DE3) Δ cysH + pET23PacysH (addition of Pseudomonas cysH) 6.8

Similarly, a strain that had the cysC gene knocked out was used to test complementation by the B. subtilis and P. aeruginosa cysH genes. Strain BL21(DE3) ΔcysC was transformed with plasmids pET23a, pET23a+cysH (B. subtilis), and pET23a+cysH (P. aeruginosa), respectively. Single colonies of the above three strains together with BL21(DE3) were inoculated in 5 mL of OnEx medium containing amino acids except L-cysteine and L-methionine. The cells were cultured at 37° C. with shaking for 48 h and growth was measure by OD_(600 nm). The results, showed in Table 15, indicated that cysH-encoded APS reductase from both B. subtilis and P. aeruginosa could complement the cysC mutation on BL21(DE3) which demonstrated that it was possible to bypass the formation of PAPS.

TABLE 15 Optical density at 600 nm of ΔcysC complementation experiments strain OD_(600 nm) ^(a) BL21(DE3) 4.5 BL21(DE3) ΔcysC + pET23a 0.0 BL21(DE3) ΔcysC + pET23a + cysH (B. subtilis) 2.5 BL21(DE3) ΔcysC + pET23a + cysH (P. aeruginosa) 4.2 ^(a)The results are the average of three cultures. Overexpression of Enzymes in the Sulfur Assimilation Pathway

As described above, to increase the production of methionine it can be helpful to have a very efficient sulfur assimilation pathway. To facilitate direct sulfhydrylation of the acylhomoserine precursor, the availability of SH₂ is essential. All of the main genes of the sulfur assimilation pathway were cloned and overexpressed in the methionine production strain TF4076BJF. The genes overexpressed were:

-   cys PUWA: sulfate permease -   cysDN: ATP sulfurylase (EC 2.7.7.4) -   CysCCys II: APS kinase and PAPS sulfotransferase (EC 2.7.1.25 and EC     1.8.4.8) -   CysIJCysG: NADPH-Sulfite reductase (EC 1.8.1.2) -   CysB: transcription activator

These genes were overexpressed in a strain containing the dual pathways metABC and metXY, and the methionine production was measured in our standard shake flask protocol. The aforementioned five groups of sulfate assimilating genes were respectively cloned into vector pCL-(Prmf) which was constructed by replacing the Plac promoter of plasmid pCL1920 with the promoter of E. coli rmf gene. The results obtained are shown in Table 16 below:

TABLE 16 Results from overexpression of various sulfur assimilation pathway enzymes Met Strains OD mg/L Met/OD TF4076BJF metYX (Lm) 8.0 934 116 TF4076BJF metYX (Lm) cysPUWA 4.2 206 49 TF4076BJF metYX (Lm) cysDN 10.3 1271 123 TF4076BJF metYX (Lm) cysCcysH 9.9 1348 136 TF4076BJF metYX (Lm) cysJIcysG 7.7 1038 134 TF4076BJF metYX (Lm) cysB 9.4 425 45

Overexpression of the transport enzymes as well as the transcription regulator resulted in lower production of methionine and a significant drop in the amount of methionine per unit of cell mass. Increasing the activity of the sulfurylase, the APS kinase and the sulfotransferase, all resulted in increased methionine production per unit of cells as well as total methionine produced. Given that these increases are observed in a strain harboring two different plasmids, it can be expected that the results will be improved much further once expression of the enzymes is tuned and optimized.

Example 4 Exemplary Methionine Production Strains

As previously described, the various genetic modifications described herein can be made through incorporation of recombinant DNA sequences independent of the chromosome, or the recombinant DNA sequences can be incorporated into the production strain chromosome. The recombinant DNA sequences can be incorporated into the host cells as a single copy or in multiple copies.

i) A microorganism, such as E. coli ATCC #13070 or TF4076, is engineered to contain a functional deletion of thrB and metJ so that the genes are attenuated. This microorganism expresses the metX and metY genes, as well as a recombinant nucleic acid sequence which causes overexpression of the native metH gene. The expression of metX and metY introduces an additional pathway in E. coli and the overexpression of the native metH gene causes an increased flux of homocysteine to methionine.

ii) Another production strain is created by making the following modifications to the microorganism described in i). The microorganism described in i), is further modified by transforming the microorganism with a recombinant DNA molecule encoding an active metZ gene, such as the one from Pseudomonas aeruginosa.

iii) Yet another production strain is created by making the following modifications to the microorganism described in i). The microorganism described in i), is further modified to replace the native metA gene with a feedback inhibition resistant metA gene, such as those described in Example 3.

iv) Another production strain is created by making the following modifications to the microorganism described in iii). The microorganism described in iii) is transformed with an active metZ gene.

v) Another production strain is created by making the following modifications to the microorganism described in i). The microorganism described in i) which overexpresses the product of the metF gene is additionally modified to attenuate the transcriptional repressor gene lacI.

vi) Additional production strains are created by making the following modifications to any of the productions strains described herein. The production strains are engineered to overexpress the genes cysDN, cysIJ, or cysCH or combinations thereof to improve sulfur assimulation. Optionally, these production strains are additionally modified to replace the native cysC and cysH from E. coli with a single cysH gene from P. aeurignosa or B. subtilis.

vii) Another production strain is made by modifying any of the production strains described herein such that the methionine importer gene metD is attenuated. 

What is claimed is:
 1. An isolated E. coli for producing a detectable amount of methionine, the isolated E. coli comprising: one or more first polypeptides comprising direct sulfhydrylation activity, wherein the one or more first polypeptides uses O-succinylhomoserine (OSHS) or O-acetylhomoserine (OAHS) as a substrate and is encoded by metZ, metY or a combination thereof; one or more second polypeptides comprising transsulfuration activity, wherein the one or more second polypeptides is encoded by endogenous E. coli metB, metC or a combination thereof; and a third polypeptide comprising homoserine O-succinyltransferase activity, wherein the third polypeptide is encoded by feedback inhibition resistant metA comprising the amino acid sequence of SEQ ID NO: 2, 4, 6, 8, or 10, wherein the direct sulfhydrylation activity arises from expression of an exogenous nucleic acid sequence of metZ, metY, or a combination thereof, and wherein metZ is obtained from Pseudomonas aeruginosa, and metY is obtained from Leptospira meyeri, Deinococcus radiodurans, Chloroflexus aurantiacus, or Pseudomonas aeruginosa.
 2. The isolated E. coil of claim 1, wherein at least one gene selected from metD, metK, metJ, thrB, serA, and combinations thereof, is attenuated.
 3. The isolated E. coil of claim 1, wherein at least one gene selected from metA, metB, metC, metE, metY, metZ, metX, metH, cysPWUA, cysD, cysN, cysC, cysH, cysI, cysJ, cysG, csyK, cysM, and combinations thereof, is over-expressed.
 4. A method of making methionine, comprising: culturing the isolated E. coli of claim 1 under conditions that permit production of methionine; and isolating the methionine.
 5. The method of claim 4, wherein the isolated E. coli further comprises a polypeptide having homoserine O-acetyltransferase activity with an amino acid sequence having at least 90% sequence identity to SEQ ID NO: 44, 45, 46 or
 47. 6. The method of claim 4, wherein the one or more first polypeptides comprises an amino acid sequence having at least 90% sequence identity to SEQ ID NO: 36, 37, 38 or
 39. 7. The method of claim 4, wherein the one or more first polypeptides comprises an amino acid sequence comprising at least 90% sequence identity to SEQ ID NO:
 40. 8. The method of claim 4, wherein the isolated E. coli further comprises at least one of an attenuated gene selected from metD, metK, metJ, thrB, serA, and combinations thereof and additional genetically engineered nucleic acid sequence changes resulting in a genetically engineered production strain, and wherein the genetically engineered production strain produces 10% more methionine compared to the microorganism without such changes.
 9. The isolated E. coli of claim 1, wherein the one or more first polypeptides comprises a nucleic acid sequence having at least 90% sequence identity to SEQ ID NO: 44, 45, 46 or
 47. 10. The isolated E. coli of claim 1, wherein the one or more first polypeptides comprises a nucleic acid sequence selected from the group consisting of SEQ ID NOs: 44, 45, 46 and
 47. 11. The isolated E. coli of claim 1, wherein the one or more first polypeptides comprises an amino acid sequence having at least 90% sequence identity to SEQ ID NO: 36, 37, 38 or
 39. 12. The isolated E. coli of claim 1, wherein the one or more first polypeptides comprise an amino acid sequence comprising at least 90% sequence identity to SEQ ID NO:
 40. 